CALCULATING FAILURE PROBABILITIES OF PASSIVE
SYSTEMS DURING TRANSIENTS
By
Francisco J. Mackay
Electronics Engineer
Academia Politecnica Naval, Chile - 2001
SUBMITTED TO THE DEPARTMENT OF NUCLEAR SCIENCE AND
ENGINEERING INPARTIAL
FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF
MASTER OF SCIENCE IN NUCLEAR SCIENCE AND ENGINEERING
AT THE
MASSACHUSETTS INSTITUTE OF TECHNOLOGY
JANUARY 2007
@2007 Massachusetts Institute ofTechnology. All rights reserved.
The author hereby grants to MIT permission to reproduce
and to distribute publicly paper and electronic
copies of this thesis documert ip whole or in part
in any medium now known
t
ereafter created.
Signature of the author: ___
Departmei-oNuclear Sciennce
YL~afu
Certified by:
.
e
Ja u ry
oogy
0
.,
George E. Apostolakis
Professor of Nuclear Science and Engineering
Thesis supervisor
Accepted by:
.
.
..
Ab
Pavel Hejzlar
PrinciRal Research Scientist
Accepted by:
MASSACHUSTS INSTITUrMJ
OF TECHNOLOGY
I
Jeffrey A. Coderre
Associate Professor of Nuclear Science and Engineering
Chairman, Department Committee on Graduate Students
OCT 12 2007
LIBRARIES
ARCHIVES
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CALCULATING FAILURE PROBABILITIES OF PASSIVE
SYSTEMS DURING TRANSIENTS
by
Francisco J. Mackay
Submitted to the Department of Nuclear Science &
Engineering on January 23, 2007 in partial fulfillment of
the requirements for the Degree of Master of Science in
Nuclear Science and Engineering
1. ABSTRACT
A time-dependent reliability evaluation of a two-loop passive Decay Heat
Removal (DHR) system was performed as part of the iterative design process for a
helium-cooled fast reactor. The system was modeled using RELAP5-3D. The
uncertainties in input parameters were assessed and were propagated through the model
using Latin Hypercube Sampling. An important finding was the discovery that the
smaller pressure loss through the DHR heat exchanger than through the core would make
the flow to bypass the core through one DHR loop, if two loops operated in parallel.
This finding is a warning against modeling only one lumped DHR loop and assuming that
n of them will remove n times the decay power. Sensitivity analyses revealed that there
are values of some input parameters for which failures are very unlikely. The calculated
conditional (i.e., given the LOCA) failure probability was deemed to be too high leading
to the identification of several design changes to improve system reliability. This study is
an example of the kinds of insights that can be obtained by including a reliability
assessment in the design process. It is different from the usual use of PSA in design,
which compares different system configurations, because it focuses on the thermalhydraulic performance of a safety function.
Thesis supervisor: George E. Apostolakis
Title: Professor of Nuclear Science and Engineering
2. ACKNOWLEDGMENT
I want to thank my wife for, without her support and care, this work could not
have been possible. To Prof. George E. Apostolakis, for his guidance, support, counsel
and for the most his patience. To Pavel Hejzlar, whose knowledge was always an
incredible source of light when walking through the dark paths of accurate simulation.
To Prof. Michael J. Driscoll, for being an unlimited source of ideas and support through
the whole process. Last, but not least, to Chris Handwerk, Mike Stawicki, David
Carpenter, Tyler Ellis, Giovanbattista Patalano, Edoardo Cavalieri, Lorene Debesse and
Rodney Busquim for their friendship and willingness to help me in so many ways. This
would not have been the same without you guys, thanks.
3. TABLE OF CONTENTS
............................................. . . . . 3
A B ST R A C T .......................................................
A C KN O W LED G M EN T ....................................................................
.................... 4
TABLE OF CONTENTS ........................................................
..................... 5
TA BLE OF FIG U R ES...............................................................................................6
INTRODUCTION...................
......................................
7
SYSTEM DESCRIPTION..................................................13
AN A L Y SIS ................................................................................................................
19
7.1.
Mechanistic Model ...................
7.2 .
Un certain ties ......................................................................................................
7.3.
Uncertainty Propagation .....................
7.4.
Failure Criteria .................................................................................................
28
7.5.
System Failure Criteria ....................................................................................
29
7.6 .
R esults...............................
......
..... .........................
.
......................... 19
24
............................................... 27
................................................. 30
8.
RISK-BASED DESIGN CHANGES ......................................................................
41
9.
C O N C LU SION S .......................................................................................................
43
10
. R EFEREN C ES .......................................................................
. . . . ..
...........
11
S APPENDICES ......................
............... 45
..................................
47
11.1.
APPENDIX A: RELAP5-3D NODALIZATION DIAGRAM ..................... 47
11.2.
APPENDIX B: RELAP5-3D NOMINAL INPUT DECK ............................ 48
11.3.
APPENDIX C: TABLE OF PROPAGATED UNCERTAITY...................157
11.4.
APPENDIX D: UTILIZED ALGORITHMS ............................................
163
4. TABLE OF FIGURES
Figure 1. An example of load and capacity stochastic processes.......................................8
Figure 2. Schem atic GFR system layout .......................................................................
13
Figure 3. Schematic of a natural circulation loop ..........................................................
15
Figure 4. RELAP5-3D Nodalization diagram of the system.........................................19
Figure 5. Possible flow patterns ...........................................
23
Figure 6 Example of the output from an LHS uncertainty propagation............................28
Figure 7 Multiple Failure Criteria...................................................................................30
Figure 8 Realizations for Maximum Temperature in the Cladding...................................31
Figure 9 Realizations for the Maximum Temperature in the Hot Leg of DHR Loops ....33
Figure 10 Leakage Threshold Effect (cladding failure) .................................................
34
Figure 11 Maximum leakage and HTCS Threshold Effect (structural failure).................36
Figure 12 Search for threshold effects (Failure Mode 1, cladding failure) ....................... 37
Figure 13 Search for threshold effects (Failure Mode 2, structural failure)......................38
5. INTRODUCTION
According to the International Atomic Energy Agency (IAEA) definition, a
passive system is either a system that is composed of passive components and structures
or a system that uses active components in a very limited way to initiate subsequent
passive operation (IAEA, 1991). Of great importance are thermal-hydraulic systems (TH) that fall under IAEA Categories B and C. These are characterized by moving working
fluids either without or with moving mechanical parts, such as check or relief valves,
respectively.
Passive system reliability analysis has attracted increasing attention over the last
decade. The expectation that the overall plant reliability should increase by replacing
certain active systems with passive ones is based on the fact that unreliability of active
systems is due primarily to the unreliability of the energy source that is required for them
to perform. Passive system functionality does not rely on an external source of energy,
but on an intelligent use of the naturally available one (gravity), which is always present.
As the research in the field advances, the tradeoffs between passive and active systems
are becoming clear. Although the energy source is always available for a passive system,
it is normally weak. As a result, passive systems are much more sensitive to changes in
the surroundings than active ones (Pagani et al, 2005). In addition, the operators cannot
control passive systems the way they can control the performance of active systems.
Since the reliability evaluation does not depend on the availability of the driving
energy, a new description of the concept of failure is required. The concept of passive
function failure, borrowed from reliability physics, has been introduced by Burgazzi
(2003). It describes "failure" in terms of a "load" exerted during the perfornnance of the
system on its components and the "capacity" of these components to withstand that load.
An example of a load is the temperature at a certain point as the system operates. The
temperature limit of the material at that point above which damage occurs is the capacity
of the system. In general, both the load and the capacity are uncertain and may depend
on time (an example is shown in Figure 1). The probability that the load exceeds the
capacity is the failure probability of the system for that point in time. Two models are
therefore needed, one for the load and one for the capacity. In general, the capacity
model may be correlated with the load model. In other words, the capacity of a
component can be a function of its state and therefore time-dependent. An example of
this is the dependence of material yield stress on temperature. Therefore, if the analyzed
component is a pipe, the pressure required to break it is a function of the temperature,
which may vary according to the performance of the system.
CAPACITY(y,t)
y
..........
MEAN VALUES
X
LOAD(x,t)
Figure 1. An example of load and capacity stochastic processes.
The following tasks need to be performed to evaluate the reliability of a passive
system:
1. Identification of the components (points in the system) where failure may occur
and their respective loads and capacities. A component may fail in a number of
ways. Failure Modes and Effects Analysis (FMEA) and Hazard and Operability
HAZOP Analysis are methods that are helpful in identifying component failure
modes (Burgazzi, 2004).
2. Definition of component failure criteria, i.e., the type of capacity model that
should be used for each load determined in the previous task. Capacity models
may be in the form of deterministic limits (e.g., imposed by a regulatory
authority) or probability distributions based on experiments and/or expert
opinions.
3. Selection of sets of parameters (boundary conditions, system properties and initial
conditions) that affect the behavior of each load determined in Task 1. The
Analytical Hierarchy Process (AHP) has been proposed to help identify these
important driving parameters (Zio et al, 2003; Marques et al, 2005).
4. Development of a probability distribution for each parameter input to the model to
represent the relevant uncertainties. This is a crucial step and is normally done
based on experiments or expert opinions (Jafari et al, 2003; Marques et al, 2005;
Pagani et al, 2005).
5. Propagation of the uncertainty distributions of the input parameters through the
models. Many techniques have been proposed to perform this step. They range
from Monte Carlo simulation (Pagani et al, 2005) to the development of response
surfaces. A discussion on the advantages and disadvantages of each option is
presented by Marques et al. (2005).
6. Calculation of system reliability. The system is considered failed if one or more
of the failure criteria are met. This means that more than one component may fail
for the same system realization (Marques et al, 2005). The result of this
calculation is the probability of failure of the system.
These tasks provide the main structure of any passive system reliability
calculation. The list does not include tasks aimed at improving the quality and efficiency
of the calculations, such as early sensitivity analyses or iteration loops between tasks. A
more detailed description of these tasks is presented in (Jafari et al, 2003; Marques et al,
2005).
This work presents a detailed description of the time-dependent reliability
evaluation of a passive decay heat removal system after a Lost-of-Coolant-Accident
(LOCA). We emphasize the difficulties found in the process, propose solutions, and
describe the lessons learned regarding the design itself. Our focus is on uncertainties and
their propagation.
A preliminary design of a helium-cooled fast reactor constitutes the case study. It
is part of the MIT studies on a Gas-cooled Fast Reactor (GFR) design. The system and
its components were simulated using RELAP5-3D (INEEL, 2001). The entire system
operates as one passive system whose initiation is triggered by the reactor scram after a
Loss-of-Coolant Accident (LOCA). Section 2 describes the system.
The complete description of the reliability calculation is presented in Section 3,
where suggestions for design improvement are also given by identifying the input
parameters that are driving the failure of the system. Finally, conclusions on different
aspects of the work and future research suggestions are provided in Section 4.
[This page is left intentionally blank]
6. SYSTEM DESCRIPTION
The GFR design considered consists of a 600 MWth helium-cooled fast reactor
core inside the Pressure Vessel (PV), a Brayton power cycle within the Power
Conversion Unit (PCU), and two 50% Decay Heat Removal (DHR) loops (Figure 2).
The core is designed to have very low pressure drop to maximize the natural circulation
capability. Moreover, the PV, the PCU and the DHR loops are surrounded by a guard
containment with a high design pressure of 2 MPa (20 bars), so that, after primary system
depressurization, the final pressure in the guard containment would be high enough to
make DHR by natural circulation of helium possible. Each DHR loop is designed to
extract 2% of the reactor nominal power (12 MWth) at a backup pressure of 1.3 MPa.
QteafEmhgnpr
........
......
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"qGuil
(-'
I..
-ýý
%fiWGOI
WAS
P CbsedA
kYhAMw
KIPr
eMR&
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Figure 2. Schematic GFR system layout.
Each DHR loop consists of two separate circuits. The first is connected to the PV
through a coaxial pipe with the cold leg running in the outside. Heat is subsequently
delivered to the second circuit, filled with water, through a heat exchanger. The water
loop delivers the heat to a pool outside the containment building. Check valves are
placed in the cold leg of the helium section of each DHR loop. The PCU contains a
Brayton power cycle with recuperator, precooler and intercooler. The shaft that is
propelled by the turbine provides energy to the generator and to the low and high
pressure compressors of the cycle as well. More details on the GFR system layout are in
Hejzlar et al. (2005).
As will be seen later, there are several parameters that are of importance for a
natural circulation loop to work properly. An intuitive review of the phenomenon gives a
good insight into the system's dynamics. Figure 3 shows a generic loop that is the
starting point of the discussion. Heat is inserted at point (1) and extracted at point (2).
There is no heat transfer at any other point in the circuit. When the fluid is heated at
point (1) its density decreases and it begins to flow up and forms the hotter fluid column
that is shown in the figure. At the same time, when heat is extracted at point (2), the
density of the fluid increases and as a result it moves down forming the colder fluid
column shown in the figure. The difference in weight (W-w) between the two columns is
the driving force that results in a certain mass flow running through the loop. The mass
flow is primarily determined by the driving force and the resistance that the system exerts
to the flow through pipes and fittings. To increase the mass flow then one can increase
H, the difference in altitude between points (1) and (2), increase the temperature
difference between the columns, or replace the fluid by one whose density change per
unit temperature is greater.
(2)
C
E
D
0
"o
-0
*0
Q5
0)
(1)
m
Figure 3. Schematic of a natural circulation loop.
Assuming the loop is at steady state (which implies Qo,, which the system is extracting heat from the source is equal to
Q,,
= 0), the rate at
[J/s]:
Q,,, = m* Cp * AT
(1)
where
m = pVA = Mass Flow [kg/s]
Cp = Isobaric Heat Capacity [J/kg K]
AT = Temperature Difference between hot and cold legs [K]
p = Density [kg/m']
V = Velocity [m/s]
A = Flowing Area [m2]
Therefore, in order to extract more heat either the mass flow or the temperature
difference needs to be increased in the passive loop. Increasing the mass flow is
normally preferable because to increase AT almost always means to increase the
temperature of the hot leg consequently reducing the safety margin on the temperature
limit. Embedded in this short argument is the importance of the backup pressure. A
greater pressure means higher density of the helium and a higher mass flow through the
heat exchanger for the same fluid velocity, letting the system extract more heat from the
source, while keeping AT constant. Although not mentioned in the discussion above, an
increase in the density is also beneficial to the natural circulation phenomenon because it
reduces the friction factor along the loop due to reduced kinematic viscosity, therefore
allowing a larger mass flow.
A LOCA on the cold leg of the PCU was chosen as the initiating event of the
analysis. The system is designed to survive a 500 cm 2 break, but it was evaluated for a 5
cm 2 break that is much more probable (frequency:
10-3 per year) than a large break. The
sequence of events is as follows:
1. The cooling function is performed by the helium coming from the PCU
from the moment of the accident until the shaft with turbine and
compressors stops. During that time the flow coming out from the PCU is
divided into two streams at the point of the rupture: the first one goes
directly to the containment through the break and the second follows its
initial path to the core through the downcomer. How long the shaft runs is
a function of the size of the break. For a 500 cm 2 break, the Brayton cycle
would work as such, propelled by the decay heat, for a period of time
ranging between 30 to 40 minutes. This gives enough time for the decay
heat to fall below the 2% nominal power threshold, so the DHR loops can
2
safely take over the cooling function. The situation is different for a 5 cm
break. The shaft stops after approximately 10 minutes. The higher
density of the helium, sustained in time because of the small break area,
plus a smaller temperature difference across the core provide more
resistance to compressors and less energy is extracted by the turbine from
helium, therefore the reduction in shaft coastdown time. During this
period the PCU is cooling down the core and the check valves placed on
the cold legs of the natural circulation DHR loops are closed.
2. Once the shaft stops, the pressure difference is reversed and the check
valves open, allowing the natural circulation through the DHR loops to
start. Two parameters are important here: the pressure inside the PV and
DHR loop and the amount of decay heat that is being released at that
moment. For the case of a 500 cm 2 break, the pressure inside the PV is
already equalized to that of the containment and the decay heat is below
the 2% nominal power threshold. Problems could arise, for example, if
the structures in the containment absorbed an excessive amount of heat,
therefore reducing the backup pressure required for natural circulation, or
if the shaft stopped when the decay heat was greater than 12 MWth. For
the 5 cm 2 break, the dynamics are different. The shaft stops within 10
minutes of the accident but the pressure inside the PV remains high
enough to sustain a natural circulation capable to extract the decay heat
that is being produced. Nevertheless, when natural circulation through the
DHR loops starts, the temperature difference across the core is not
sufficient to extract the decay heat that is being produced, so the outlet
temperature begins to rise until it reaches its operating condition.
Meanwhile, the natural circulation is continually deteriorating by the
depressurization process that will eventually end about 30 to 40 minutes
after the accident. After that time the decay heat is below the 12 MWth
mark and, if the backup pressure is by then adequate and decaying slower
than the decay heat, the system will be operating safely.
7. ANALYSIS
7. 1.MechanisticModel
The mechanistic model simulates the dynamic behavior of the system given a set
of boundary and initial conditions and system physical properties (i.e., it is the "model of
the world" in PRA terminology (Apostolakis, 1994)). This model will be used to perform
sensitivity analyses and to propagate the uncertainties in the input parameters.
A complete model of the system was built using RELAP5-3D (INEEL, 2001).
RELAP5-3D is a thermal-hydraulic code developed by Idaho National Laboratory for the
analysis of accidents in nuclear power plants. Figure 4 shows the nodalization of the
model of the system.
INU I I U
Ly
-
daL
Figure 4. RELAP5-3D Nodalization diagram of the system
The DHR loops are on the top left area of the diagram and show the water and
helium sides connected together by heat exchangers. Heat exchangers are represented by
rectangles enclosing the volumes involved in the heat transfer balance. The reactor is
immediately below the DHR loops. Two long vertical volumes represent the downcomer
and, in the center of the core, two channels can be distinguished between the lower and
upper plenums; one representing the average and the other the hottest channels in the
core. On the lower right-hand corner, the PCU is modeled. The turbine and both highand low-pressure compressors are connected to the same shaft. There are three heat
exchangers in this part of the model and they correspond to the recuperator, the precooler and the intercooler. Finally, enclosed by a dashed line circle is the valve that
simulates the rupture generating the LOCA. This valve connects the outlet of the cold leg
of the PCU to the volume that represents the containment building.
The following is a list of modeling information relevant to the results:
1. The ANS 79 Decay Heat Model is used (ANS, 1979)
2. All pipe walls are modeled for pipes in each DHR loop. The importance of
this practice comes from the fact that the heat capacity of steel is greater than
that of helium. A significant amount of mass flow is required then to either
heat them up or cool them down, therefore affecting the transient behavior of
the natural circulation loops (Hejzlar et al, 2005).
3. The core is modeled by two channels: an average and a hot one. The hot
channel simulates the hottest channel in the core in accordance to the core's
peaking factor. Attached to each channel, there are heat structures simulating
cladding and fuel. This configuration allows the monitoring of the highest
temperature in both fuel and cladding.
4. RELAP5-3D does not allow negative angular velocity for shafts and
compressor operation at negligibly small flows. To overcome this issue and
continue with calculations beyond this point, as soon as the mass flow
entering the PCU becomes smaller than 0.5% of the nominal flow, the PCU is
isolated from the rest of the system and an auxiliary external flow is injected
into it to keep the shaft running with positive angular velocity, while the rest
of the simulation is carried on in parallel. This action prevents simulation of
the effect of bypass flow through the PCU on core cooling; hence the failure
probabilities reported here are optimistic assuming that PCU can be isolated
with 100% reliability.
5. Leakage of the check valves in the DHR loops is simulated with a timedependent junction running parallel to the respective check valve. A timedependent junction allows the implementation of a constant negative mass
flow rate through the loop, if the pressure drop across the check valve is
positive. Otherwise, the mass flow rate is zero.
6. The heat transfer from the water loop to the pool outside the containment
building is simulated with a natural convection boundary condition with a
fixed T (bulk temperature of the pool) equal to the ambient temperature.
7. Three heat structures simulating the containment liner, the concrete on the
floor, and the equipment inside the containment building are added to the
containment hydrodynamic volume. Their effect is important because they
absorb heat reducing the temperature of the helium in the containment and
thus the backup pressure.
During the mechanistic analysis, several unexpected effects were discovered. The
system was initially designed with two 50% DHR loops that would work in parallel (see
flow pattern (1) in Figure 5). This feature needed to be changed because the check valves
of one of the DHR loops would never be open at the same time except for short periods
of unstable flow. The reason for this behavior is the smaller pressure drop through the
DHR heat exchangers than through the core and flow tendency to bypass the core through
one of the DHR loops closing check valve on this loop. Thus, if both valves are forced to
open, one of the loops would finally work backwards (see flow pattern (2), Loop 2, in
Figure 5); stealing the mass flow from the core so that most of the flow from the correctly
operating loop proceeds through the common lower plenum to the other loop and
ultimately to the upper plenum. Such core bypass reduces substantially core flow rate
and rapidly leads to fuel overheating. To overcome this problem, the design was
modified to increase the original 2x50% capacity to 2x100% capacity DHR loops.
Furthermore, the appearance of this phenomenon clearly emphasizes the importance of
modeling the DHR loops separately instead of lumping them up into one loop that
extracts as much energy as the sum of the individual loops.
25 m
I
3)
(1)
DINJ I I U •vL.,,•LC
Figure 5. Possible flow patterns.
Another interesting phenomenon happens if the check valves are forced to open
before the mass flow that is injected by the compressors on mounted on the coasting
down shaft stops. In this case, both loops would work backwards (see flow pattern (3) in
Figure 5) because the pressure in the upper plenum would be smaller than that in the
lower plenum. This unintended behavior is stable at least for the decay heat levels that
occur during the first three hours after the accident. The same phenomenon is observed if
there is a leaky check valve. During normal operation the pressure difference across the
core produces a continuous flow through the leaking check valves. If the leakage of the
check valves is sufficiently high, the continuous leak forces the flow through the
emergency heat exchangers where it experiences cooling and the originally hot riser
becomes cooler than the downcomer resulting the in the continuous reversed flow. After
the shaft stops, both loops continue in reversed operation mode and the sum of leaking
flows is not sufficient to cool the core thus leading to failure.
As discussed earlier, the heat absorption from the structures inside the
containment building was expected to have an impact on the evolution of its pressure and
therefore on the backup pressure once the PV and the containment pressures are
equalized. The results from a sensitivity analysis on this parameter showed that the liner
needed to be isolated and the free volume to be reduced.
After these changes to the design, the model is ready for the next stage on the
analysis: uncertainty analysis.
7.2. Uncertainties
As stated in the introduction, passive systems are sensitive to changes in the
boundary and initial conditions and to changes in the numerical values of the parameters
that define the system properties. All these conditions and parameters are called input
parameters. This sensitivity is due primarily to the weakness and uncontrollability of the
driving force, gravity.
A set of six input parameters were selected to be propagated through the model.
Table 1 shows these parameters and their probability distribution functions. The
selection was made based on sensitivity analyses done on several parameters and expert
opinion.
INPUT
DISTRUBUTION EXTREME VALUES
PARAMETER
ETERPECNLS
PARAM
Core
Roughness
Roughness
Lognormal
LOWER
UPPER
1.00E-05
1.00E-04
UNITS
EXTREME VALUES
CORRESPOND TO
PERCENTILES
LOWER
[m]
UPPER
5
85
DHR1 Leakage
Check Exponential
Valve
-
0.50 [kg/s]
80
DHR2
DHR2 Check
Check
-
0.50 [kg/s]
80
Valve Leakage
Exponential
Valve Leakage
Heat Transfer
Coefficient,
Coefficient,
Lognormal
0.50
2.00 [Dimensionless]
Containment
20
75
20
80
20
80
Structures
Moment of
Inertia of the
Shaft
Normal
Core Heat
Transfer
Coefficient
Lognormal
656.88
0.40
802.86 [kg*m2]
1.60 [Dimensionless]
Table 1 Selected Input Parameters and their probability distributions
Roughness in the Core refers to the roughness of the surfaces in the core that are
in contact with helium. Even though it is small in absolute terms, the pressure drop in the
core accounts for about 70% of the overall pressure drop along the DHR loops under
nominal operation. An increase in the roughness translates into a larger pressure drop in
the core with the consequent reduction in the mass flow rate. As the mass flow rate
decreases, the required temperature difference across the core increases for the same
amount of heat removal.
Check Valve Leakage: The first assumption is that the check valves are always
leaking. The effect of leakage is to delay the opening the valves. A backward flow
through the DHR loops is present during normal operation and during the time the PCU
is cooling the core after the accident, therefore the system has to overcome the inertia of
that flow in order to open the check valves once the PCU has stopped.
Heat Transfer Coefficient of Structures in the ContainmentBuilding (HTCS): The
result of having a greater HTCS is that blown down helium in the containment is cooled
down faster and therefore reducing the pressure that at the same point in time the
containment would have had under adiabatic conditions. Since this is a preliminary
design, the containment layout and geometry and positions of internal structures inside
are not known. Each modeled structure corresponds to the lumping of several objects
and each of these would have its own time-dependent heat transfer coefficient, so the
modeled HTCS correspond to average values. Furthermore, RELAP5-3D calculates the
heat transfer coefficient for each structure in the containment volume according to its
respective boundary condition, so the uncertainty is represented by a multiplicative factor
that modifies the HTCS calculated by the code.
Heat Transfer Coefficient in the Core (HTCC): The effect of a smaller heat
transfer coefficient is that a greater temperature gradient across the core would be
required in order to remove the same amount of heat. In this case, there is uncertainty in
heat transfer correlations implemented RELAP5-3D in calculating the correct value of
heat transfer coefficient under low-Reynolds number, high heat-flux flows where local
buoyancy and acceleration forces can significantly reduce heat transfer coefficient (Lee
and Hejzlar, 2006). The uncertainty is represented by a multiplicative factor that
modifies the HTCC calculated by the code.
Moment oflnertia of the Shaft: A shaft with a greater moment of inertia is more
difficult to decelerate and therefore could run longer. This is important because as the
coastdown time is increased, the moment at which the DHR loops are initiated is also
increased placing the system in a safer operating condition with a smaller decay heat.
7.3. UncertaintyPropagation
Monte Carlo simulation is used to propagate the uncertainties in the input
parameters through the model. In order to reduce the number of trials, Latin Hypercube
Sampling (LHS) was employed. In short, this technique divides the six-dimensional
probability defined by the input parameters into a set of equiprobable six-dimensional
cubes (hypercubes) from which the samples are then chosen. The fundamental
assumption of the method is that the input variables are independent. Since only one
sample point is chosen from each hypercube, the sample points are equiprobable. More
information on LHS can be found in Helton and Davis (2003).
Once the sample is chosen, a RELAP5-3D simulation is made for each unique set
of sample points (one from each hypercube). Each set defines a scenario. Since these
sets are equiprobable, the corresponding results of RELAP5-3D are also equiprobable. A
three-hour time span starting at the moment of the accident was chosen as the simulation
interval. This selection was made based on sensitivity analyses that showed that the
pressure in the containment becomes equal to the pressure in the PV (consequently, the
flow through the rupture is negligible) after two hours. The pressure rate of change
inside the containment was never less than -17 Pa/s at the end of three hours. The
sensitivity analyses also showed that the temperature gradient at the same point was
never less than -9.0x 10-3 K. Furthermore, the power that is being generated at the core by
then is about 6.8 MWth, well below the design specifications of the DHR loops. For the
present work, it is assumed that the containment has no leakage.
7.4. FailureCriteria
After the simulations are finished, a screening of the output parameters is again
required in order to define which of them are going to be considered for the unreliability
evaluation. It is important to do so because new failure modes may be discovered in the
process. Figure 6 shows an example (not an actual result) for an output parameter. Each
curve corresponds to a particular scenario (set of sample points).
OP
time
Figure 6 Example of the output from an LHS uncertainty propagation
The next step is to define the failure criterion for each selected output parameter.
In traditional reliability assessments, this task is done much earlier in the process and in
fact it can be made during the mechanistic analysis, after structuring the set of potentially
relevant output parameters, but it must be reviewed here because new failure modes may
have been discovered. The failure criteria used in this work are deterministic limits such
as the horizontal dashed line shown in Figure 6. Any realization that exceeds the limit is
considered a failure. Since all realizations are equally likely, the probability of failure
during the time span of the graph is equal to the number of curves that exceed the limit
divided by the total number of curves.
To write this down more formally, let A(i) be a binary variable that is equal to
unity when the ith scenario (realization) leads to failure and equal to zero otherwise.
Then, the probability of failure is:
M
PFs
XA(i)
MM
(2)
where M is the total number of realizations.
7.5. System FailureCriteria
Multiple failure criteria should be used whenever more than one output parameter
may lead to failure. This means that a specific scenario may lead to no failure or at least
one failure. The overall failure probability can be calculated as follows:
Let AI, A 2 ,...AN be the failure vectors associated to N failure modes over M
realizations. Define F(i) = max(A, (i), A 2 (i),..., AN (i)) Vi e {1,2,3,...,M}, then the mean
probability of multiple failure PF is define as:
M
PFI,-
IF(i)
M
(3)
Figure 7 shows an example of this procedure.
Realization i
1
Al
A2
A3
...
AN
Max()
1
F
1
2
1
3
0
4
Failure Probability
M
5
M
Figure 7 Multiple Failure Criteria
7.6. Results
After reviewing the parameters of the system at various points, two failure modes
were finally selected for the reliability evaluation of the system: Cladding damage in the
hot channel and structural failure in the hot legs of the DHR Loops. A limit of 1600 °C
(1873 K) was set as the maximum temperature for cladding damage. It is assumed that
the silicon carbide cladding would release fission products if that temperature were
exceeded. The imposed limit on the DHR pipe walls is 850 TC (1123 K). It is assumed
that the DHR loop would suffer a structural collapse if this limit were exceeded leading
to the loss of mass flow rate through the core. Figure 8 shows 128 realizations for the
maximum cladding temperature. The horizontal dashed line corresponds to the
previously mentioned limit.
Maximum Iemperature in tne UlaOing
-v
-
------------........
4001
"
A
,
.
1000
B
1
1
1
2000
3000
4000
1
5000
l
I
6000
Time (s)
C
..
........
I
I
I
7000
8000
9000
i
100000
Figure 8 Realizations for Maximum Temperature in the Cladding
As expected, the maximum temperature in the cladding occurs after the shaft
stops (about 500 seconds after the LOCA - Point A in Figure 8). During this period, the
mass flow rate through the core reaches its minimum and the helium in the core,
becoming less dense because of the increasing temperature, tries to overcome the
negative flow coming down from the leaking (both check valves are assumed to leak) of
the DHR loops. Eventually, one of the DHR check valves opens (Point B in Figure 8)
initiating the natural circulation through the core and the maximum temperature in the
cladding reduces its rate of change and ultimately comes down (Point C in Figure 8). It is
during this last period of time when realizations reach their maxima. There is one
realization for which the temperature never comes down and corresponds to the only case
in which the check valves never open because of the significant leakage in both of them.
There were 15 curves that exceeded the limit, so the overall probability for this failure
mode is 0.12. This probability is conditional on the LOCA.
The second failure mode corresponds to the structural failure of the operating
DHR Loop. As already stated, a limit of 850 C (1123 K) to the maximum temperature on
the hot legs (MTHL) was set as the failure criterion for this failure mode. Figure 9 shows
the 128 resulting realizations. Each realization is represented in the graph by two curves;
one for each DHR loop. The always decreasing curves correspond to the DHR loop with
the check valve closed. In the initial conditions of the simulation, the MTHL is set as if
there were no leakage in either loop. This is the worst possible initial condition because
the MTHL is smaller with leakage than without. This is due to the fact that the leaking
helium comes from the downcomer and passes through water cooled heat exchanger
where it cools down substantially. There were 26 curves that exceeded the limit, thus the
calculated conditional probability for this failure mode is 0.20.
Maximum Temperature in the Hot Leg of DHR Loops
1200
-j
T
T
3000
4000
FT
F'F
1100
1000
900
)
800
E
700
I-600
500
400
300
i
1000
A
2000
B
5000
6000
7000
8000
9000
10000
Time (s)
Figure 9 Realizations for the Maximum Temperature in the Hot Leg of DHR Loops
As soon as the LOCA occurs, the MTHL starts decreasing in both loops because
of the injection of cold helium from the downcomer. When the check valve opens (Point
A in Figure 9), the behavior of the operating loop starts departing from the one that is still
leaking until it reaches a minimum at about 30 minutes (Point B in Figure 9). The reason
is that, once the valve opens, natural circulation starts building up and hotter helium
coming from the upper plenum heats up the pipes. From then on, the MTHL is well
correlated to the behavior of the maximum temperature in the cladding presented in
Figure 8.
The conditional failure probability is 0.305 when both failure modes are included.
Referring to the discussion in Section 3.5, we find that
F = 39 over a total of 128
realizations. There were 15 and 26 failures for each respective failure mode, therefore
the total would be 41 instead of 39, if each realization led to a single failure. We
conclude that two realizations led to failures by both failure modes.
3.7 Insights
Interesting insights into the behavior of the system can be produced by developing
scatter plots of failures and successes for two parameters at a time (Ghosh and
Apostolakis, 2006). Figure 10 shows such a plot for the two leakages associated with
each Monte Carlo realization (one for each DHR loop) for the maximum temperature in
the cladding. On the horizontal axis we plot the maximum of the two leakages and on the
vertical axis the minimum. The plus signs indicate a realization and the square around a
plus sign indicates that this realization is, in fact, a failure of the cladding. Looking at the
lower left corner of the plot we observe that no failures exist below the dashed line.
Thus, we conclude that no cladding failure occurs when the maximum leakage in the
loops is less than about 0.8 kg/s and the minimum leakage is less than about 0.5 kg/s.
0.8
O.6
06
I
Ii
E3
-000.4
0.2
19n
co
0.5
CD
.
4
+.
. . _ ..,
:,.
if,:•,_-.:*•.
1 •-• +1
,
I
02
[
-•
II
I
-
0.6
L0.4
0B
1
1.2
Max(Leakage
1, Leakage2) [kg/s]
l
14
1.6
Figure 10 Leakage Threshold Effect (cladding failure)
1.8
The explanation for this behavior is the following: After the shaft stops, the
system attempts to open the check valves by overcoming the leakage. The valve with the
smallest leakage is the one that eventually opens. The higher the minimum leakage the
later the check valve opens. Such a delay means that more heat has been deposited in the
core with no extraction and therefore the temperature has increased.
Once the valve opens, natural circulation develops through the corresponding
DHR loop, but part of the fluid in the lower plenum is taken by the other DHR loop's
leakage and transferred directly to the upper plenum, thus bypassing the core. The higher
the maximum leakage, the smaller mass flow is available to the core for heat removal.
Failure is the combined effect of the two quantities and, as Figure 10 shows, only values
outside the lower triangle can lead to failure.
Threshold effects can be found for the structural failure mode as well. Figure 11
shows a similar plot for the effect of the HTCS and the maximum leakage of the valves.
The effect of the leakage is easily understood. The maximum leakage corresponds to the
loop whose check valve never opens and remains leaking after the other DHR loop starts
operating. That flow is inserting cold helium to the inlet of the operating DHR loop
through common upper plenum. Thus, if the maximum leakage is sufficiently high, it
cools down the upper plenum enough, preventing failure. As Figure 11 shows, there is
no structural damage when the HTCS factor is larger than 0.86 and the maximum leakage
is larger than 0.63 [kg/s]. Figure 11 also shows that there is no cladding damage when
the HTCS factor is smaller than 0.86 regardless of the value of the maximum leakage.
The explanation for this behavior is as follows: the lower the HTCS, the higher the
pressure in the containment and, therefore, inside the PV after the pressures are
equalized. Higher pressure means higher helium density and, as explained in Section 2
(Equation 1), this corresponds to a smaller temperature difference across the core for the
same amount of extracted heat. Finally, the smaller temperature difference is translated
into a smaller core outlet temperature that reduces the probability of failure by MTHL.
It'llT'
iu
+
-10
U1
U) 10
~,i14
.E_
01
to
~1
C/)
+
10'
1011
0
1
0.2
0!4
0!6
0.8
1
I
Max(Leakage 1,Leakage 2) [kg/s]
1.2
1.4
I
1.6
1.8
Figure 11 Maximum leakage and HTCS Threshold Effect (structural failure)
Insights into the behavior of the system can also be produced using the
Generalized Sensitivity Analysis (GSA) developed in (Hornberger and Spear, 1981) for
environmental systems. A GSA application to nuclear waste repositories is in (Ghosh
and Apostolakis, 2006). GSA partitions Monte Carlo realizations into two bins: one bin
contains all the realizations leading to failure and the other all the realizations not leading
to failure. We then look at the realizations in the failure bin and ask whether there are
any threshold effects, i.e., intervals of values of the input parameters that guarantee no
failure. The process will become clear using concrete examples.
Figure 12 shows the cumulative distribution function of the parameter on the
horizontal axis in the realizations that did not lead to cladding failure (continuous curve)
and the cumulative distribution function in the realizations that did lead to such failure
(staircase curve). Only the parameter HTCS shows a potential threshold effect in the
sense that failure would be very unlikely if the HTCS factor were less than about 0.48.
'--7
0.9
0.8
0.70.6
I
-,
.1
-'I
"
10
1"
105
4
10
0.5
0.4
0.3[
-I
0.2
0.1
f•t
.
2
.
.
10,
. . ........."
.
.
. .....
.
.
•
.
. . ....
10'
10
10
.
i t f lit
HTCS (Dimensionless)
Roughness (m)
1..
4-
/
.
.V
/
/
'4
A
.2
0
1011
o
HTCC (Dimensionless)
10'
500 50
600 6
700 750 800 850 9
950 1000
Shaft Moment of Inertia (kg m2)
Figure 12 Search for threshold effects (Failure Mode 1, cladding failure)
Figure 13 shows the same type of graphs for the second failure mode (structural
failure). This time, the threshold effect on the HTCS is more pronounced. Failure only
occurs if the value of the HTCS factor is greater than about 0.86, as found earlier (Fig.
10).
0.91
_
0.8
j
0.9-
08
0.7-.
0.7
0.6
0.6
0.5
0.5
0.4
0.3
1
/
0.2
01
'
0.4
0.3
0.2
0.1
0
10
10
10
10
102
10'
10
10
102
HTCS (Dimensionless)
Roughness (m)
1[
0.8
0.7
0.86
0.5
0.4
0.3
0.2
0.1
10
0
10
HTCC (Dimensionless)
101
500
550
600
650
700
750
800
850
900
950
Shaft Moment of Inertia (kg m2)
Figure 13 Search for threshold effects (Failure Mode 2, structural failure)
Both failure modes present threshold effects for the HTCS. Both failure modes
become very unlikely for small values of the HTCS factor because the pressure in the
containment can be maintained high for a longer period of time. This confirms an earlier
finding by Pagani et al., (2005) that containment pressure is a key parameter for the
success of natural circulation decay heat removal in gas cooled systems. Also, it is
important to note that containment leakage, which was not part of our studies, is another
important parameter that will negatively affect system performance in a similar manner
as HTCS. On the other hand, for check valve leakage, what is beneficial for one failure
mode is not for the other. To prevent failure due to melting of the cladding, a small
maximum check valve leakage is desirable; but to prevent a structural collapse of the
DHR loops, a large maximum leakage is preferred.
[This page is left intentionally blank]
8. RISK-BASED DESIGN CHANGES
The failure probability of 0.305 (conditional on the LOCA occurrence) is deemed
to be too high. Since a good amount of information about the system behavior under
different scenarios has been gathered, several actions can be taken. Since the dominant
failure mode is the structural collapse of a DHR loop (accounts for -2/3 of the total
failure probability), it is there where the first design change can be made. In the design
analyzed, the hot legs were simulated with adiabatic heat flux boundary conditions at the
outer periphery, which effectively corresponds to perfect insulation at this surface. The
design has been modified by placing the insulation on the inner surface of the pipe. This
way, the outer perimeter is cooled down by the cold leg flow (recall that cold leg is a
coaxial pipe surrounding the hot leg). However, heat losses through the insulation heat
up the cold leg flow reducing the buoyancy driving head and affecting the natural
circulation capability. Therefore, this solution also requires raising containment backup
pressure to achieve desired DHR performance.
Additional design changes are necessary to reduce the failure probability. The
backup pressure is a relatively strong factor on both failure modes since threshold effects
are visible for the HTCS factor in both failure modes, though they are of different
magnitudes. Therefore, an increase in containment backup pressure would substantially
reduce the failure probability. One possible way to achieve this is to insulate the steel
structures in the containment to minimize heat transfer to these structures and their effect
on pressure decrease. Another option is a gradual depressurization of the helium
inventory storage tanks, which are part of the system and have a large helium coolant
inventory, into the containment. However, an increase in containment design pressure
with an associated cost increase would be required.
The primary concerns are the check valve leakage and core bypass phenomena
because of their strong effect on the performance of the passive system as a whole. The
use of more reliable check valves is of great significance to this design, but most
important is the observation that the redundancy of DHR loops can actually impair the
performance of the DHR system because the parallel loop can itself become a bypass.
Therefore, the smaller than 100% capacity DHR loops cannot be used and 100% capacity
loops are necessary. Nevertheless, any leak of check valves in parallel loops affects the
cooling capability of the core negatively. Thus, use of just one 100% DHR loop with a
reliable and leak-proof check valve would eliminate the possibility of core bypass and
provide the best performance, but such a solution is unrealistic since no perfect valves
exist. Consequently, the use of a combination of active and passive systems for DHR or
of a fully active DHR with reliable backup power need to be considered and, in fact, may
provide lower failure probabilities.
9. CONCLUSIONS
From an overall perspective, the first important conclusion is that the passive
system design process has to incorporate a reliability assessment. The complexity of the
system and the overall impact of the simultaneous variation of several input parameters
makes it impossible for the designer to foresee every possible situation.
The reliability evaluation process provides useful information to the designer. At
an early stage, the analysis of the system components gives a starting point as to where
the hazards may be; the most insightful view, however, comes later with the second and
third screenings during the mechanistic analysis and after the uncertainty propagation.
During the mechanistic analysis, improvements to the design can be made in view of the
evidence given by nominal simulations and sensitivity analyses. The probabilistic
analysis produces insights that the nominal analysis does not produce. In Figures 8 and
9, the curves that exceed the damage limits are the results of specific combinations of the
values of the input parameters. The curves corresponding to the nominal values are
below the limits and do not reveal the possibility of failure. In addition, the sensitivity
analysis allows the discovery of threshold effects in the input parameters and the
potential combined effect of two of them in two-dimensional scatter plots.
We point out that the probabilistic analysis presented here is different from the
usual use of PSA in design. In the latter case, several design configurations are analyzed
and compared using a metric such as the core damage frequency (Mizuno et al, 2005;
Delaney et al, 2005). These studies are performed at the system level and usually lead to
changes in the redundancy and diversity of the system. The present work uses a
mechanistic model for a safety function and investigates the impact of uncertainties in the
input parameters on the probability of function failure. This process reveals the
significance of certain possible values of the input parameters and leads to design
changes that affect these values. It is closer to the analysis presented by Ghosh and
Apostolakis (2006) for nuclear waste repositories.
The sensitivity analyses identify potential threshold effects in the input parameters
and lead to a better understanding of the dynamics of the system. This understanding is
very helpful in efforts to improve the design in an effective way. Since one design
change may affect the behavior of several failure modes differently, it is crucial to
understand their interactions for the success of the design improvement. Finally, the
single failure probabilities and the safety function failure probability provide a
framework within which to assess the impact of design changes quantitatively.
10.REFERENCES
ANS, 1979. American National Standardfor Decay Heat Power in Light Water
Reactors, ANSI/ANS-5.1-1979, American Nuclear Society, La Grange
Park, Illinois.
Apostolakis, G.E., 1994. "A commentary on model uncertainty," in: Proceedingsof
Workshop on Model Uncertainty:Its Characterizationand Quantification,
Annapolis, MD, October 20-22, 1993. A. Mosleh, N. Siu, C. Smidts, and
C. Lui, Eds., Report NUREG/CP-0138, US Nuclear Regulatory
Commission, Washington, DC.
Burgazzi, L., 2003. "Reliability evaluation of passive systems through functional
reliability assessment." Nuclear Technology, 144:145-151.
Burgazzi, L., 2004. "Evaluation of uncertainties related to passive systems
performance." Nuclear Engineeringand Design, 230:93-106.
Delaney, M.J., Apostolakis, G.E., and Driscoll, M.J., 2005. "Risk-informed design
guidance for future reactor systems." NuclearEngineeringand Design,
235:1537-1556.
Ghosh, S. T., Apostolakis, G.E., 2006. "Extracting risk insights from performance
assessments for high-level radioactive waste repositories." Nuclear
Technology, 153:70-88.
Hejzlar, P., Kim, S.J., and Williams, W.C., 2005. TransientA THENA/RELAP5-3D
Calculationsfor a 600MWth Plate-Type Helium GFR, MIT Report MITGFR-026, Massachusetts Institute of Technology, Cambridge, MA.
Helton, J.C., Davis, J.F., 2003. "Latin hypercube sampling and the propagation of
uncertainty in analyses of complex systems." ReliabilityEngineering &
System Safety, 81:23-69.
Hornberger, G.M., Spear, R.C., 1981. "An approach to the preliminary analysis of
environmental systems." JournalofEnvironmentalManagement, 12:7-18.
IAEA, 1991. Safety Related Terms for Advanced Nuclear Power Plants, TEC-DOC626. International Atomic Energy Agency, Vienna, Austria.
INEEL, 2001. RELAP5-3D©code manual volume I: code structure,system models,
and solution methods. INEEL-EXT-98-00834, Idaho National
Engineering and Environmental Laboratory, Idaho Falls, Idaho.
Jafari, J., D'Auria, F., Kazeminejad, H., Davilu, H., 2003. "Reliability evaluation of
a natural circulation system." NuclearEngineeringand Design, 224:79104.
Lee, J.I., and Hejzlar, P., 2007. "Experimental and Computational Analysis of Gas
Natural Circulation Loop", Proceedings of the International Congress on
Advances in Nuclear Power Plants ICAPP '07, Paper 7381, Nice, France,
May 13-18.
Marques, M, Pignatel, J.F., Saignes, P., D'Auria, F., Burgazzi, L., Miller, C., BoladoLavin, R., Kirchsteiger, C., La Lumia, V., and Ivanov, I., 2005.
"Methodology for the reliability evaluation of a passive system and its
integration into a probabilistic safety assessment." Nuclear Engineering
andDesign, 235:2612-2631.
Mizuno, Y., Ninokata, H., and Finnicum, D.J., 2005. "Risk-informed design of IRIS
using a level-1 probabilistic risk assessment from its conceptual design
phase." Reliability Engineeringand System Safety, 87:201-209.
Pagani, L.P., Apostolakis, G.E., and Hejzlar, P., 2005. "The impact of uncertainties
on the performance of passive systems," Nuclear Technology, 149:129140.
Zio, E, Cantarella, M, Cammi, A., 2003. "The analytic hierarchy process as a
systematic approach to the identification of important parameters for the
reliability assessment of passive systems." Nuclear Engineeringand
Design, 226:311-336.
11. APPENDICES
11.1.
APPENDIX A: RELAP5-3D NODALIZA TION DIAGRAM
11.2.
APPENDIX B: RELAP5-3D NOMINAL INPUT DECK
MIT-GCFR Plate DHR
100 newath transnt
101 run
102 si si
105 5.0 6.0
110 air
115 1.0
*
g=1, no noncond
120 100010000 0.0 he primary 1
121 133010000 0.0 h2o h2opc 1
122 143010000 0.0 h2o h2oit 1
123 700010000 0.0 h2o uhsloopl
124 701010000 0.0 h2o uhsloop2
*crdno end time min dt max dt control
201
10800.0
1.0-10 0.0025
23
-
minor ed
400
major ed
800000
*
*
*
*--------------------------------------------------------*
MINOR EDITS
*---------------------------------------------------------
*
*---------------------------------------------------------
*
Reactor Coolant System
*--------------------------------------------------------*
301
302
303
304
305
306
307
308
309
310
311
312
313
314
315
316
317
318
319
320
321
322
*
*
p
tempf
p
tempf
p
tempf
p
tempf
mflowj
mflowj
cntrlvar
cntrlvar
cntrlvar
cntrlvar
p
tempf
p
tempf
p
tempf
p
tempf
750010000
750010000
751010000
751010000
750200000
750200000
751200000
751200000
750010000
751010000
126
127
128
129
710010000
710010000
711010000
711010000
710050000
710050000
711050000
711050000
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
*
Water Loops Data
q
q
q
q
from
from
from
from
710
711
750
751
restart
400000
323
324
325
326
327
328
329
330
331
332
333
334
335
336
337
338
339
340
341
342
343
344
345
346
347
348
650010000
651010000
650050000
p
P
651050000
p
g
650010000
tempg
651010000
tempg
650050000
tempg
tempg
651050000
mflowj
665000000
mflowj
674000000
cntrlvar 120
cntrlvar 125
P
610050000
p
tempg
610050000
611050000
p
tempg
611050000
666010000
p
tempg
666010000
676010000
p
tempg
676010000
666050000
p
tempg
666050000
676050000
p
tempg
676050000
httemp
610100101
httemp
611100101
DHR Loops Data
p
P
p
*
*
*
*
*
*
*
*
*
*
*
*
*
349
350
351
352
353
354
355
356
357
358
359
360
361
362
363
364
365
367
368
369
370
371
372
373
374
375
376
377
378
p
p
p
p
tempg
tempg
tempg
tempg
p
p
p
p
tempg
tempg
tempg
tempg
mflowj
mflowj
mflowj
mflowj
mf 1owj
p
tempg
p
tempg
cntrlvar
cntrlvar
cntrl1var
cntrlvar
250010000
251010000
250080000
251080000
250010000
251010000
250080000
251080000
670010000
670080000
800010000
800080000
670010000
670080000
800010000
800080000
250010000
251010000
670010000
800010000
300040000
300050000
300050000
100010000
100010000
111
102
123
110
Reactor and
Downcomer Data
Q extracted from rector
Estimated Q extracted
Q generated by the reactor
Max temp fuel 251 httemp
* MAx temp clad
379
cntrlvar 103
380
381
382
383
mflowj
sonicj
p
tempg
062000000
062000000
070010000
070010000
* Break and Containment Data
mflowj
p
tempg
cntrlvar
mflowj
cntrlvar
mflowj
mflowj
turvel
cntrlvar
cntrlvar
082000000
520300000
520300000
40
550010000
42
580010000
597010000
510
32
34
*
251 httemp
*
384
385
386
387
388
389
390
391
392
393
394
20800001
sonicj
PCU Data
*
*
*
*
*
*
*
* Turbine velocity rad/s
* q from pc
* q from ic
062000000
*---------------------------------------------------------
*
TRIPS
*--------------------------------------------------------*
20600000 expanded
*Time to be taken for Steady-State: 50 seconds
20603500 time 0 ge timeof 522 5. n * trip LP cmpr, HP cmpr
Turbine
timeof 522 5. 1 * generator trip
20603600 time
null 0 5.e6 1 * open bypass valve
20604810 time
null 0 1.0e6 1 * close bypass valve
20604820 time
20605010 time 0 ge timeof 522 5. 1 *@Rx Trip'
20605010 time 0 ge timeof 501225.
1
-.
*@Rx Trip'
*20605020 time 0 ge timeof 501 0.0 1 -1. *@Rx Trip'
lt
ge
ge
and
null 0 5.e6 n *trpvlv from tmdpvol
null 0 5. 1 *break junction (valve 062)
timeof 522 180. n
20605210
20605220
20605230
time
time
time
20605240
20605250
20605260
20605270
20605280
20605290
20605300
20605310
20605320
cntrlvar 102
time 0 ge
time 0 it
time 0 it
cntrlvar 110
time 0 ge
time 0 ge
time 0 lt
vlvarea 665
it cntrlvar 123 -2.e6 n
n *valves connecting DHRs to 670
null 0 0.
null 0 5. n *OPEN valve 685 & 686
null 0 5. n *open valve 082
gt null 0 900. n
timeof 1003 0. 1 *connect external torque
null 0 20000. n
null 0 20000. n
eq null 0 0. n
20605340
vlvarea 674
eq
20605350
20605360
turvel
mflowj
null 0 0. n
510 it null 0 0.01 n
597010000 gt null 0 1.67
*trip cprssrs
n
20605370
20605380
20605390
20605400
20605410
20605420
20605430
mflowj
time 0
p
p
p
p
time 0
082000000 le null 0 1.67 n
gt null 0 10. n
690010000 ge p
698010000
691010000 ge p
694010000
690010000 lt p
698010000
691010000 lt p
694010000
ge timeof 522 40. n
20610010
20610020
20610030
20610040
20610050
20610060
530
530
523
525
537
524
534 n
532 n
1006 1
1005 n
538 1
528 n
and
and
and
xor
and
and
0.
0.
0.
0.
n
n
n
n
*valve 694
*valve 692
*close valve 082
*open vlvs 593 & 503
*open vlvs 501 & 591
*
*
**%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
**
%
**
HYDRODYNAMIC COMPONENTS
**
%
%
**%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
*
PRIMARY COOLANT SYSTEM
*
*--------------------------------------------------------*-------------------------------------------
*
Reactor Inlet Plenum
*---------------------------------------------------------
*
name
1000000
*
pipe
number of volumes
1000001
*
pipe/annulus
rx-in-pl
area
5
no of vol
1000101 6.7117 5
*
length no of vol
1000301 0.2
5
*
volume no of vol
1000401 0.0
5
*
azi ang no of vol
1000501 90.
5
*
ver ang no of vol
1000601 90.
5
*
elev. no of vol
1000701 0.1
5
*
rough dhydr. no of vol
1000801 1.0Oe-5 0.15 5
*
kforw kbackw no of jun
1000901 0.0
0.0
4
*
v-flag no of vol
1001001
00000
5
*
j-flag no of jun
1001101 000000 4
*
cntrl pressure temperature * * * no of vol
1001201 0
7152053. 2310826. 2310826. 1. 0. 1
1001202 0
7152044. 2310826. 2310826. 1. 0. 2
7152034. 2310826. 2310826. 1. 0. 3
1001203 0
7152024. 2310826. 2310826. 1. 0. 4
1001204 0
7152014. 2310826. 2310826. 1. 0. 5
1001205 0
cntrl
*
1001300 0
*
w/v.liq w/v.vap w/v.int no of jun
1001301 9.97593 9.97593 0.
1 * 319.2105
2 * 319.2105
1001302 9.97594 9.97594 0.
3 * 319.2105
1001303 9.97595 9.97595 0.
4 * 319.2105
1001304 9.97596 9.97596 0.
*---------------------------------------------------------
*
Junction: Reactor Inlet Plenum to Lower Reflector
*---------------------------------------------------------
*
name
junction
2080000 rip-lrc sngljun
to
area kforw kbackw j-flag
*
from
2080101 100050002 210000000 1.39801 0.23
*
cntrl w/v.liq w/v.vap w/v.int
2080201 0 47.4743 47.4743 0. * 316.416
0.23
0000000
*
*---------------------------------------------------------
*
Junction: Reactor Inlet Plenum to Lower Reflector
*---------------------------------------------------------
name
junction
*
2090000 rip-lrh sngljun
area kforw kbackw j-flag
*
from
to
2090101 100010000 211000000 0.01259 0.23
*
cntrl w/v.liq w/v.vap w/v.int
2090201 0 46.5594 46.5594 0. * 2.79462
0.23
0000000
*---------------------------------------------------------
*
Reactor Inlet Reflector
*---------------------------------------------------------
volume
*
name
2100000 in-rflt snglvol
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
2100101 1.39801 1.0 0.0 90.0 90.0 1.0 1.0e-5 0.0127 000000
*
cntrl press temp
7140967. 2311218. 2311218. 1.
2100200 0
*
*---------------------------------------------------------
*
Reactor Inlet Reflector Hot Channel
*---------------------------------------------------------
volume
name
*
2110000 in-rfhc snglvol
*
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
2110101 0.01259 1.0 0.0 90.0 90.0 1.0 1.0e-5 0.0127 000000
*
cntrl press temp
7141388. 2311206. 2311206. 1.
2110200 0
*
*---------------------------------------------------------
*
Junction: Reactor Inlet Reflector to Core
*---------------------------------------------------------
*
name
junction
2150000 irf-cor sngljun
*
from
to
area kforw kbackw j-flag
2150101 210010000 250000000 1.39801 3.00
*
cntrl w/v.liq w/v.vap w/v.int
2150201 0 47.5237 47.5237 0. * 316.416
0.00
0000000
*
*---------------------------------------------------------
*
Junction: Reactor Inlet Reflector to Core Hot Channel
*---------------------------------------------------------
*
name
junction
2160000 irf-chc sngljun
*
from
to
area kforw kbackw j-flag
2160101 211010000 251000000 0.01259 3.00
*
cntrl w/v.liq w/v.vap w/v.int
2160201 0 46.6061 46.6061 0. * 2.79462
0.00
*
*---------------------------------------------------------
*
Reactor Core
*---------------------------------------------------------
*
name pipe/annulus
2500000 rx-core pipe
*
number of volumes
2500001 8
*
area no of vol
2500101 1.39801 8
*
length no of vol
2500301 0.24375 8
*
volume no of vol
2500401 0.0
8
*
azi ang no of vol
2500501 90.
8
*
ver ang no of vol
2500601 90.
8
*
elev. no of vol
2500701 0.24375 8
*
rough dhydr. no of vol
2500801 1.0e-5 0.0127 8
*
kforw kbackw no of jun
2500901 0.0
0.0
7
*
v-flag no of vol
2501001 00000 8
*
j-flag no of jun
2501101 000000 7
*
cntrl pressure temperature
2501201 0
7118911. 2407030.
2501202 0
7116096. 2541886.
2501203 0
7113010. 2703636.
2501204 0
7109660. 2879407.
2501205 0
7106074. 3055207.
2501206 0
7102302. 3217043.
2501207 0
7098412. 3352028.
2501208 0
7094483. 3449417.
*
cntrl
2501300 0
* * *
2407030.
2541886.
2703636.
2879407.
3055207.
3217043.
3352028.
3449417.
no
1.
1.
1.
1.
1.
1.
1.
1.
of vol
0. 1
0. 2
0. 3
0. 4
0. 5
0. 6
0. 7
0. 8
0000000
*
w/v.liq w/v.vap w/v.int no of jun
2501301 49.585 49.585 0.
1 * 316.416
2501302 52.3795 52.3795 0.
2 * 316.416
3 * 316.416
2501303 55.7317 55.7317 0.
4 * 316.416
2501304 59.3765 59.3765 0.
5 * 316.416
2501305 63.0252 63.0252 0.
2501306 66.3886 66.3886 0.
6 * 316.416
7 * 316.416
2501307 69.2
69.2
0.
*---------------------------------------------------------
*
Reactor Core Hot Channel
*---------------------------------------------------------
*
name pipe/annulus
2510000 rx-core pipe
*
number of volumes
2510001 8
area no of vol
*
2510101 0.01259 8
length no of vol
*
2510301 0.24375 8
*
volume no of vol
2510401 0.0
8
*
azi ang no of vol
2510501 90.
8
ver ang no of vol
*
2510601 90.
8
*
elev. no of vol
2510701 0.24375 8
*
rough dhydr. no of vol
2510801 1.0e-5 0.0127
8
*
kforw kbackw no of jun
2510901 0.0
7
0.0
*
v-flag no of vol
2511001 00000 8
*
j-flag no of jun
2511101 000000 7
*
cntrl pressure temperature
2511201 0
7120148. 2423867.
2511202 0
7117354. 2582030.
2511203 0
7114255. 2771736.
2511204 0
7110856. 2977891.
2511205 0
7107192. 3184081.
7103315. 3373888.
2511206 0
2511207 0
7099301. 3532202.
2511208 0
7095240. 3646411.
*
cntrl
2511300 0
w/v.liq w/v.vap w/v.int
*
2511301 48.9652 48.9652 0.
2511302 52.1772 52.1772 0.
2511303 56.0307 56.0307 0.
2511304 60.2206 60.2206 0.
2511305 64.4151 64.4151 0.
2511306 68.2815 68.2815 0.
2511307 71.5131 71.5131 0.
*
no
*
*
*
2423867.
2582030.
2771736.
2977891.
3184081.
3373888.
3532202.
3646411. 1. 0.
jun
2.79462
2.79462
2.79462
2.79462
2.79462
2.79462
2.79462
vol
1
2
3
4
5
6
7
8
*-------------------------------------------------------
*
Junction: Reactor Core to Outlet Reflector
*---------------------------------------------------------
junction
*
name
2550000 cor-orf sngljun
from
to
area kforw kbackw j-flag
*
2550101 250010000 290000000 1.39801 3.00
*
cntrl w/v.liq w/v.vap w/v.int
2550201 0 71.2362 71.2362 0. * 316.416
0.00
0000000
*
*---------------------------------------------------------
*
Junction: Reactor Core Hot Channel to Outlet Reflector
*---------------------------------------------------------
name
junction
*
2560000 cor-ohc sngljun
to
area kforw kbackw j-flag
*
from
2560101 251010000 291000000 0.01259 3.00
*
cntrl w/v.liq w/v.vap w/v.int
2560201 0 73.853 73.853 0. * 2.79462
0.00
0000000
*
*--------------------------------------------------------*
Reactor Outlet Reflector
*---------------------------------------------------------
*
name volume
2900000 o-rflt snglvol
*
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
2900101 1.39801 1.0 0.0 90.0 90.0 1.0 1.0e-5 0.0127 000000
*
cntrl press
temp
2900200 0
7061007. 3448288. 3448288. 1.
*
*---------------------------------------------------------
*
Reactor Outlet Reflector HC
*--------------------------------------------------------*
name volume
2910000 o-rflt snglvol
*
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
2910101 0.01259 1.0 0.0 90.0 90.0 1.0 1.0e-5 0.0127 000000
*
cntrl press
temp
2910200 0
7061106. 3645208. 3645208. 1.
*
*---------------------------------------------------------
*
Junction: Reactor Core to Outlet Plenum
*---------------------------------------------------------
*
name
junction
2920000 cor-orf sngljun
*
from
to
area kforw kbackw j-flag
2920101 290010000 300000000 0.0 0.46 0.46
*
cntrl w/v.liq w/v.vap w/v.int
2920201 0 71.4177 71.4177 0. * 316.416
0000000
*
*---------------------------------------------------------
*
Junction: Reactor Core Hot Channel to Outlet Plenum
*---------------------------------------------------------
*
name
junction
2930000 cor-ohc sngljun
*
from
to
area kforw kbackw j-flag
2930101 291010000 300000000 0.0 0.46 0.46
0000000
*
cntrl w/v.liq
2930201 0 74.045
w/v.vap w/v.int
74.045 0. * 2.79462
*---------------------------------------------------------
*
Reactor Outlet Plenum
*---------------------------------------------------------
*
name pipe/annulus
3000000 rx-o-pl pipe
*
number of volumes
3000001 5
*
area no of vol
3000101 43.0080 5
*
length no of vol
3000301 0.2
5
volume no of vol
*
3000401 0.0
5
azi ang no of vol
*
5
3000501 90.
*
ver ang no of vol
5
3000601 90.
*
elev. no of vol
3000701 0.20
5
*
rough dhydr. no of vol
3000801 4.5e-5 7.4
5
kforw kbackw no of jun
*
4
0.0
3000901 0.0
*
v-flag no of vol
3001001 00000 5
*
j-flag no of jun
3001101 000000 4
*
cntrl pressure temperature * * * no of
7058110. 3449668. 3449668. 1. 0.
3001201 0
7058104. 3449667. 3449667. 1. 0.
3001202 0
7058098. 3449666. 3449666. 1. 0.
3001203
0
7058092. 3449666. 3449666. 1. 0.
3001204 0
0
7058085. 3449665. 3449665. 1. 0.
3001205
*
cntrl
3001300 0
w/v.liq w/v.vap w/v.int no of jun
*
1 * 319.2105
3001301 2.34353 2.34353 0.
2 * 319.2105
3001302 2.34353 2.34353 0.
3 * 319.2105
3001303 2.34353 2.34353 0.
4 * 319.2105
3001304 2.34353 2.34353 0.
vol
1
2
3
4
5
*---------------------------------------------------------
*
Junction: Plenum to Pressure controller
*---------------------------------------------------------
junction
*
name
*3200000 cor-orf valve
area kforw kbackw
from
to
*
*3200101 300010000 340000000 1.e5
*
cntrl w/v.liq w/v.vap w/v.int
312.20 0.0
*3200201 1 0.
*crdno valve type
*3200300 trpvlv
*crdno open trip
521
*3200301
j-flag
0. 1.e9
0000000
*
*--------------------------
-------------
-
*
Reactor Pressure Controller
*---------------------------------------------------------
*
name
volume
*3400000 rx-vent tmdpvol
*
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
*3400101 500.0 100.0 0.0 0.0 0.0 0. 0.00046 7.4 000000
*
cntrl
*3400200 003
*
press temp
*3400201 0.0 6.94220e6 1122.15
*
*---------------------------------------------------------
*
RPV Downcomer #1
*---------------------------------------------------------
*
name pipe/annulus
6700000 hp-hxcl pipe
*
number of volumes
6700001 8
*
area no of vol
6700101 3.62855 8
*
length no of vol
6700301 1.05625 8
*
volume no of vol
6700401 0.0
8
azi ang no of vol
*
6700501 -90.
8
*
ver ang no of vol
6700601 -90.
8
elev. no of vol
*
6700701 -0.68125 8
*
rough dhydr. no of vol
6700801 4.5e-5 0.6
8
*
kforw kbackw no of jun
6700901 0.0
0.0
7
*
v-flag no of vol
6701001 00000 8
*
j-flag no of jun
6701101 000000 7
*
cntrl pressure
temperature
6701201 0
7151890.
2310802.
6701202 0
7151917.
2310805.
6701203 0
7151944.
2310808.
6701204 0
7151971.
2310812.
6701205 0
7.152+6
2310816.
6701206 0
7152025.
2310819.
6701207 0
7152052.
2310823.
6701208 0
7152079.
2310827.
*
cntrl
6701300 0
*
w/v.liq w/v.vap w/v.int no
6701301 9.22622 9.22622 0.
1
6701302 9.22622 9.22622 0.
2
6701303 9.22621 9.22621 0.
3
6701304 9.2262 9.2262 0.
4 *
6701305 9.2262 9.2262 0.
5 *
6701306 9.2262 9.2262 0.
6 *
6701307 9.22619 9.22619 0.
7
* * *
2310802.
2310805.
2310808.
2310812.
2310816.
2310819.
2310823.
2310827.
of jun
* 319.2105
* 319.2105
* 319.2105
319.2105
319.2105
319.2105
* 319.2105
no
1.
1.
1.
1.
1.
1.
1.
1.
of vol
0. 1
0. 2
0. 3
0. 4
0. 5
0. 6
0. 7
0. 8
*
*-------------------------------------------------------
*
RPV Downcomer #2
*---------------------------------------------------------
*
name pipe/annulus
8000000 hp-hxcl pipe
*
number of volumes
8000001 8
*
area no of vol
8000101 3.62855 8
*
length no of vol
8000301 1.05625 8
volume no of vol
*
8000401 0.0
8
*
azi ang no of vol
8000501 -90.
8
ver ang no of vol
*
8000601 -90.
8
elev. no of vol
*
8000701 -0.68125 8
*
rough dhydr. no of vol
8000801 4.5e-5 0.6
8
kforw kbackw no of jun
*
8000901 0.0
0.0
7
v-flag no of vol
*
8001001 00000 8
j-flag no of jun
*
8001101 000000 7
temperature
*
cntrl pressure
8001201 0
7151890.
2310802.
2310805.
7151917.
8001202 0
8001203 0
7151944.
2310808.
8001204 0
7151971.
2310812.
8001205 0
7.152+6
2310816.
7152025.
2310819.
8001206 0
8001207 0
7152052.
2310823.
8001208 0
7152079.
2310827.
*
cntrl
8001300 0
w/v.liq w/v.vap w/v.int no
*
1
8001301 9.22622 9.22622 0.
8001302 9.22622 9.22622 0.
2
8001303 9.22621 9.22621 0.
3
8001304 9.2262 9.2262 0.
4 *
8001305 9.2262 9.2262
0.
5 *
6 *
8001306 9.2262 9.2262 0.
7
8001307 9.22619 9.22619 0.
*
*
*
vol
1
2
3
4
5
6
7
8
2310802.
2310805.
2310808.
2310812.
2310816.
2310819.
2310823.
2310827.
of jun
* 319.2105
* 319.2105
* 319.2105
319.2105
319.2105
319.2105
* 319.2105
-
*--------------------------------------------------
*
Junction:
-
-------
*-----------------------------------------------------
*crdno
6850000
---
Pressure Controller to RPV Downcomer
name
type
j-contr valve
*
*crdno from
to
area
jefvcahs
6850101 680000000 670000000 1.0 0. 0.
6850110 0.6 0.0 1.0 1.0
00000100
-
*crdno var flowf flowg velj
6850201 0
0. 0.
0. * 0.
*crdno valve type
6850300 trpvlv
*crdno open trip
6850301
526
*
*---------------------------------------------------------------*
Junction:
Pressure Controller to RPV Downcomer
*----------------------------------------------------------------
*crdno
6860000
name
type
j-contr valve
*
*crdno
6860101
6860110
*crdno
6860201
*crdno
6860300
*crdno
6860301
from
to
area
jefvcahs
680000000 800000000 1.0 0. 0.
0.6 0.0 1.0 1.0
var flowf flowg velj
0
0. 0.
0. * 0.
valve type
trpvlv
open trip
526
00000100
*
*---------------------------------------------------------
*
Pressure Controller for steady state
*---------------------------------------------------------
*
name
volume
6800000 p-contr tmdpvol
*
area length vol. a.ang. in.ang. elev. rough. hDe v-flag
6800101 500.00 100.0 0.0 0.0 0.0 0. 0.00046 7.4 000000
*
cntrl
6800200 3
*
press temp
6800201 0.0 7.08000e6 761.15
*--------------------------------------------------------*
SNGLJ: RPV Cold Duct to Rx Inlet Plenum
*---------------------------------------------------------
*
name
junction
6750000 cd-iplm sngljun
*
from
to
area kforw kbackw j-flag
6750101 670010000 100000000 0.0 1.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
6750201 0 9.97592 9.97592 0. * 319.2105
0000001
*
*---------------------------------------------------------
*
SNGLJ: RPV Cold Duct to Rx Inlet Plenum
*---------------------------------------------------------
*
name
junction
8010000 cd-iplm sngljun
*
from
to
area kforw kbackw j-flag
8010101 800010000 100000000 0.0 1.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
8010201 0 9.97592 9.97592 0. * 319.2105
*
**
Name Valve
5010000 bypass tmdpjun
0000001
*
from
to
5010101 500000000 502000000
cntrl trp
*
5010200 1
1005
5010201 -0.* 0. 0. 0.
5010201 -0. 0. -0. 0.
5010202
0. 0. -10. 0.
area
0.00
j-flag
0000000
*
*---------------------------------------------------------
*crdno
5020000
name
cprbp2
type
tmdpvol
*
*crdno
5020101
area lngth vol
.9104 0 0
78.
h-a v-ang delz
0. .0 0 1.5
rgh dhy
00010
*
*crdno ebt
5020200 3
*crdno time
5020201 0.0
*
500
press temp
5.e6 1150.
Hot Duct volume
*
*crdno
5000000
name
type
hotduct
pipe
*
*crdno no.vols.
4
5000001
*
*crdno area
5000101 1.606
vol.no.
4
*
*crdno length
5000301 1.85
vol.no.
4
*
*crdno v-ang
5000601 0.0
vol.no.
4
*
*crdno rough
5000801 0.
dhy
1.43
vol.no.
4
*
*crdno
5000901
ff
10.
rf
0.
jun.no.
3
*
*crdno tlpvbfe
5001001 10010
vol.no.
4
*
*crdno jefvcahs
5001101 0000000
jun.no.
3
*
*crdno
5001201
5001202
5001203
5001204
ebt pressure
0 7001960.
0 6939344.
0 6876488.
0 6813382.
temp qual vol.no.
3442779. 3442779. 1.
3434540. 3434540. 1.
3425628. 3425628. 1.
3415980. 3415980. 1.
0.
0.
0.
0.
1
2
3
4
pvbfe
*crdno i.c.
5001300 0
*
*crdno flowf flowg
velj jun.no.
0.
1 * 319.2105
5001301 62.9543 62.9543
0.
2 * 319.2105
5001302 63.1902 63.1902
0.
3 * 319.2105
5001303 63.4479 63.4479
*crdno dhy
5001401 1.43
1.0
jun.no
1.0 1.0
*------------------------------------
*hydro
5100000
component name component type
turbine
turbinel
*-----------------------------------------------------------------
$
*
no. juns vel/flow
5100001 1
0
length
area
*hydro
0.4857
4.2
5100101
volume
0.0
*
*hydro
5100102
horz angle
vert angle
90.0
4.2
0.0
*hydro
5100103
roughness
6.0e-4
delta z
fe
10
hyd diam
0.7864
*hydro ebt pressure tempe
5100200 0 3335696. 2520473. 2520473. 1.
from to
area Kf Kr efvcahs
*
5101101 500010000 510000000 0.193 0.555 0.555
*
velf
velg veli
5101201 530.307 530.307 0. * 319.2105
speed iner fric shaft trip sep eff
*
600 0
5100300 376.991 5478.2 0.39
type
*
*-
-
-
eff
2
5100400
-
-
-
-
radius
r
0.93
-
0.6
0.5
-
0000010
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
- ==
-
-===
-
*crdno name type
5150000 trbout branch
5150001 2
0
5150101 0.5
1.3848 0.0
5150102 0.0
-90.0 -1.3848
5150103 0.0 0.7979
11000
5150200 0
2944520. 2419992. 2419992. 1.
*crdno from
to
area floss rloss flag
5151101 510010000 515000000 0.0 3.0 0.0 000100
5152101 515010000 520000000 0.0 3.0 0.0 000000
*crdno flowf flowg velj
5151201 345.128 345.128 0. * 319.2105
5152201 357.214 357.214 0. * 319.2105
*
*------------------------------------*
- ===
-
- ===
- ===-
-- ===
5200000
rc-hot
pipe
*------------------------------------------------------------------
*
no. vols
5200001 30
vol area
*
5200101 10.98 30
*
length
5200301 0.09384 30
volume
*
5200401 0.0 30
azim angle
*
5200501 0.0 30
incl angle
*
5200601 -90.0 30
*
roughness hyd dia
5200801 0.3-6 2.4384e-3 30
*
kf
kr
5200901 0.0
0.0 29
*
pvbfe
5201001 00000 30
*
fvcahs
5201101 001000 29
temp
*
ebt press
5201201 0 2706427. 2322732.
5201202 0 2706121. 2286169.
5201203 0 2705834. 2249496.
5201204 0 2705555. 2212712.
5201205 0 2705283. 2175820.
5201206 0 2705019. 2138822.
5201207 0 2704762. 2101724.
5201208 0 2704513. 2064526.
5201209 0 2704272. 2027234.
5201210 0 2704037. 1989851.
5201211 0 2703810. 1952383.
5201212 0 2703588. 1914833.
5201213 0 2703366. 1877206.
5201214 0 2703143. 1839506.
5201215 0 2702920. 1801740.
5201216 0 2702696. 1763912.
5201217 0 2702473. 1726028.
5201218 0 2702250. 1688096.
5201219 0 2702027. 1650121.
5201220 0 2701805. 1612112.
5201221 0 2701583. 1574077.
5201222 0 2701362. 1536022.
5201223 0 2701141. 1497958.
5201224 0 2700922. 1459893.
5201225 0 2700704. 1421836.
5201226 0 2700487. 1383799.
5201227 0 2700272. 1345792.
5201228 0 2700059. 1307826.
5201229 0 2699848. 1269914.
5201230 0 2699634. 1232069.
vel/flow
*
5201300 0
*
liquid vapor int-face
2322732.
2286169.
2249496.
2212712.
2175820.
2138822.
2101724.
2064526.
2027234.
1989851.
1952383.
1914833.
1877206.
1839506.
1801740.
1763912.
1726028.
1688096.
1650121.
1612112.
1574077.
1536022.
1497958.
1459893.
1421836.
1383799.
1345792.
1307826.
1269914.
1232069.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
1.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
1 * 319.2105
5201301 16.6594 16.6594 0.
2 * 319.2105
5201302 16.39818 16.39818 0.
3 * 319.2105
5201303 16.13603 16.13603 0.
4
*
319.2105
5201304 15.873 15.873 0.
5 * 319.2105
15.60912
15.60912
0.
5201305
6 * 319.2105
5201306 15.3444 15.3444 0.
7 * 319.2105
5201307 15.0789 15.0789 0.
8 * 319.2105
5201308 14.8126 14.8126 0.
9 * 319.2105
5201309 14.54556 14.54556 0.
10 * 319.2105
5201310 14.2778 14.2778 0.
11 * 319.2105
5201311 14.00935 14.00935 0.
12 * 319.2105
5201312 13.74027 13.74027 0.
13 * 319.2105
5201313 13.4706 13.4706 0.
14 * 319.2105
5201314 13.20037 13.20037 0.
15 * 319.2105
5201315 12.92963 12.92963 0.
16 * 319.2105
5201316 12.6584 12.6584 0.
17 * 319.2105
5201317 12.38676 12.38676 0.
18 * 319.2105
5201318 12.11472 12.11472 0.
19 * 319.2105
5201319 11.84234 11.84234 0.
20 * 319.2105
5201320 11.56968 11.56968 0.
21 * 319.2105
5201321 11.29678 11.29678 0.
5201322 11.02372 11.02372 0.
22 * 319.2105
23 * 319.2105
5201323 10.75055 10.75055 0.
24 * 319.2105
5201324
10.47733 10.47733 0.
25 * 319.2105
5201325 10.20414 10.20414 0.
26 * 319.2105
9.93105 9.93105 0.
5201326
27 * 319.2105
5201327 9.65813 9.65813 0.
9.38548 9.38548 0.
28 * 319.2105
5201328
29 * 319.2105
5201329 9.11317 9.11317 0.
*hydro jun diam beta intercept slope jun
5201401 2.4384e-3 0.0 1.0 1.0 29
*
*crdno
5220000
name
rc-pr
type
sngljun
*
*crdno from
to
5220101 520010000
area floss rloss
525000000 0.0 0.
flag
0.
*crdno ctl flowf flowg velj
5220201 0 194.1553 194.1553 0. * 319.2105
*Inlet
*
pipe to precooler
Inlet pipe to precooler
*
*crdno
5250000
name
pr-in
type
pipe
*
*crdno no.vols.
5250001
3
*
*crdno area
5250101 0.5
*crdno length
*crdno length
vol.no.
3
vol.no.
100
5250301
3.65
*
*crdno v-ang
5250601 -90.0
vol.no.
3
*
*crdno rough dhy
5250801 0. 0.7979
vol.no.
3
*
*crdno
5250901
ff
0.
rf
0.
jun.no.
2
*
*crdno tlpvbfe
5251001 10010
vol.no.
3
*
*crdno jefvcahs
5251101 0000000
jun.no.
2
*
*crdno
5251201
5251202
5251203
ebt pressure
0 2614938.
0 2613621.
0 2613715.
temp qual vol.no.
1219848. 1219848. 1. 0. 1
1219651. 1219651. 1. 0. 2
1219665. 1219665. 1. 0. 3
*crdno i.c.
5251300 0
*
*crdno flowf flowg
velj jun.no.
0.
1 * 319.2105
5251301 197.139 197.139
0.
2 * 319.2105
5251302 197.187 197.187
*
*crdno dhy
5251401 0.7979
1.0
jun.no
1.0 1.0
*
*crdno
5280000
name
type
pr-inj sngljun
*
*crdno from
to
5280101 525010000
area floss rloss
530000000 0.0 0.
flag
0.
100
*
*crdno ctl flowf flowg velj
5280201 0 197.1838 197.1838 0. * 319.2105
*
*-------------------------------------
5300000
precool
pipe
*------------------------------------------------------
*
no. vols
5300001 20
*
vol area
5300101 28.4 20
length
*
5300301 0.2365 20
volume
*
5300401 0.0 20
*
azim angle
5300501 0.0 20
--------
*
incl angle
5300601 -90.0 20
roughness hyd dia
*
5300801 4.0e-3 9.924e-3 20
kf
kr
*
5300901 80.0 80.0
*
pvbfe
5301001 00000 20
fvcahs
*
5301101 001000 19
*
ebt press temp
5301201
2615890. 1179799 1179799. 1.
5301202
2614262. 1144789 1144789. 1.
2612682. 1114443 1114443. 1.
5301203
5301204
2611144. 1088112 1088112. 1.
5301205
2609642.
1065244 1065244. 1.
5301206
2608171. 1045368 1045368. 1.
5301207
2606727. 1028078 1028078. 1.
5301208
2605307. 1013029 1013029. 1.
2603907. 999923. 999923. 1.
5301209
5301210
2602526. 988503. 988503. 1.
5301211
2601159. 978549. 978549. 1.
2599806. 969869. 969869. 1.
5301212
5301213
2598464. 962299. 962299. 1.
2597133.
955695. 955695. 1.
5301214
2595810. 949934. 949934. 1.
5301215
2594495. 944906. 944906. 1.
5301216
2593187. 940519. 940519. 1.
5301217
5301218
2591884. 936692. 936692. 1.
5301219
2590586. 933352. 933352. 1.
2589292. 930439. 930439. 1.
5301220
*
vel/flow
5301300 0
*
liquid vapor int-face
5301301 3.35547 3.35547 0. 1 * 319.2105
5301302 3.25721 3.25721 0. 2 * 319.2105
5301303 3.17212 3.17212 0. 3 * 319.2105
5301304 3.09839 3.09839 0. 4 * 319.2105
5301305 3.03445 3.03445 0. 5 * 319.2105
5301306 2.97898 2.97898 0. 6 * 319.2105
5301307 2.93084 2.93084 0. 7 * 319.2105
5301308 2.88905 2.88905 0. 8 * 319.2105
5301309 2.85277 2.85277 0. 9 * 319.2105
5301310 2.821274 2.821274 0. 10 * 319.2105
5301311 2.79394 2.79394 0. 11 * 319.2105
5301312 2.'77023 2.77023 0. 12 * 319.2105
5301313 2.74967 2.74967 0. 13 * 319.2105
5301314 2.73186 2.73186 0. 14 * 319.2105
5301315 2.716445 2.716445 0. 15 * 319.2105
5301316
2.70312 2.70312 0. 16 * 319.2105
5301317 2.691623 2.691623 0. 17 * 319.2105
5301318 2.68172 2.68172 0. 18 * 319.2105
5301319 2.673206 2.673206 0. 19 * 319.2105
*hydro jun diam beta intercept slope jun
5301401 9.924e-3 0.0 1.0 1.0 19
$*-
*crdno
5350000
name
pr-lp
type
sngljun
*crdno from
to
5350101 530010000
area floss rloss
540000000 0.0 0.
flag
0.
100
*
*crdno ctl flowf
5350201 0 31.481
flowg velj
31.481 0. * 319.2105
*
*====
*
===
====
===
===
====
===
===
====
===
====
Inlet pipe to low pressure compressor
*
*crdno
5400000
name
type
pipe
ip-in
*
*crdno no.vols.
3
5400001
*
*crdno area
5400101 2.405
5400102 5.983
vol.no.
2
3
*
*crdno length
5400301 2.45
5400302 2.38
vol.no.
2
3
*
*crdno v-ang
vol.no.
3
90.0
5400601
*crdno rough d
*crdno rough dl hy
vol.no.
2
5400801 0.5e-5 1.75
3
5400802 0.5e-5 2.76
*
*crdno
5400901
ff rf
0. 0.
jun.no.
2
*
*crdno tlpvbf e
5401001 10000
vol.no.
3
*
*crdno
5401101
5401102
jefvcahs
0000000
0000100
jun.no.
1
2
*
*crdno
5401201
5401202
5401203
ebt pressure
0 2586328.
0 2586201.
0 2587093.
*
*crdno i.c.
5401300 0
*
temp qual vol.no.
930098. 930098. 1. 0. 1
930087. 930087. 1. 0. 2
930191. 930191. 1. 0. 3
===
===
====
===
===
*crdno flowf flowg
velj
jun.no.
0.
1 * 319.2105
5401301 31.4988 31.4988
5401302 31.4997 31.4997
0.
2 * 319.2105
*
*crdno dhy
5401401 1.75
1.0
jun.no
1.0 1.0
2
*
*
*
*
Low pressure compressor
*
*----------------------------------------------------------------------
5500000
lpcmpr
cprssr
*----------------------------------------------------------------------
*
*crdno nj
5500001 2
volume
area
length
*
5500101 0.4762
4.2
0.0
*
azim angle incl angle delta z pvbfe
00000
90.0
4.2
5500102 0.00
*
from jun area Kf
Kr fvcahs
0.0 001000
5500108 540010000 0.0 0.0
*
to
jun area Kf
Kr fvcahs
0.0 001000
5500109 560000000 0.0 0.0
*
hyd dia beta y-int slope
5500110 0.0000 0.00 1.00 1.00
5500111 0.0000 0.00 1.00 1.00
*
ebt
5500200 3 4.35e6 377.6
*
vel/flow liquid vapor int-face
312.0 0.
5500201 1
0.0
312.0 0.
0.0
5500202 1
*
id mtr vel trip rvrs
*5500301 0 -1
0 350 0
5500301 0 -1
-1 350 0
*
rated vel sp ratio flow sound inertia density
5500302 376.991 1.000 319.21 781.48 2891.44 4.2425
*
mot coeff-tf2 coeff-tf0 coeff-tfl coeff-tf3
5500303 0.0 0.0
0.0
0.0
0.0
*
shaft trip
5500309 600 535
*
5500310 0. 1000. -0.00001
*----------------------------------------------------------------------
$
* performance curves based directly on mit calculations with
* extrapolations to boundary of adjacent curves; pump efficiencies
* performance data tables
*crdno Rel Spd
nu
*
Speed
5500910 -0.10
3
*
-37.6991
5500911 0.00
4
*
0.0 rad/s
5500912 0.40
11
*
150.7694
5500913 0.50
14
*
188.4955
5500914 0.60
15
*
226.1946
5500915 0.70
16
*
263.8937
5500916 0.80
15
*
301.5928
5500917 0.90
47
*
339.2919
5500918 1.00
35
*
376.9910
5500919 1.10
36
*
414.6901
5500920 1.20
5
*
452.3892
5500921 1.30
5
*
490.0883
5500922 1.40
4
*
527.7874
5500923 1.50
4
*
565.4865
S relative
pr eta pump -10% speed
5501001 -0.1000 0.9000 0.0009 *1.0000
5501002 0.0000 0.8500 0.0009
*0.9701
5501003 0.4216 0.6285
0.0009 *0.9619
*
relative pr eta pump 0% speed
5501101 -0.1000 0.9300 0.0009
5501102 0.0000 1.0000 0.0009 *1.0000
5501103 0.3736 0.7347 0.8448 *0.9701
5501104 0.4216 0.7285 0.6275 *0.9619
*
relative pr eta pump 40% speed
5501201 -0.1000
0.9500 0.0009
5501202 0.0000 1.1000 0.0009 ********
5501203 0.3736 0.8171 0.8448 *1.0789
5501204 0.3745 0.8164 0.8436 *1.0779
5501205 0.3753
0.8158 0.8433 *1.0771
5501206 0.3762
0.8149 0.8423 *1.0759
5501207 0.3770 0.8141 0.8410 *1.0749
5501208 0.3919 0.8006 0.8127 *1.0570
5501209 0.4067
0.7868 0.7546 *1.0388
5501210 0.4216
0.7728 0.6275 *1.0204
5501211 0.4826 0.7157 0.1053 *0.9450
*
relative pr eta pump 50% speed
5501301 0.0000 1.3000 0.0009 ********
5501302 0.3736 0.9769 0.8769 *1.2898
5501303 0.4026 0.9423 0.8752 *1.2442
5501304 0.4106 0.9328 0.8747 *1.2316
5501305 0.4186 0.9232 0.8734 *1.2189
5501306 0.4266 0.9139 0.8717 *1.2066
5501307 0.4346 0.9036 0.8703 *1.1930
5501308 0.4426 0.8940 0.8688 *1.1804
5501309 0.4506 0.8844 0.8657 *1.1677
5501310 0.4586 0.8742 0.8613 *1.1542
5501311 0.4666 0.8644 0.8562 *1.1413
5501312
0.4746 0.8543
0.8499 *1.1279
5501313 0.4826 0.8445 0.8422 *1.1150
5501314 0.5941 0.7087
0.7363 *0.9357
*
relative pr eta pump 60% speed
5501401 0.0000 1.5000 0.0009 ********
5501402 0.4026 1.1765 0.8643 *1.5533
5501403 0.4613 1.0935 0.8745 *1.4438
5501404 0.4723
1.0779 0.8763 *1.4232
5501405 0.4834 1.0612 0.8765 *1.4011
5501406 0.4945 1.0447 0.8770 *1.3793
5501407 0.5055 1.0292 0.8782 *1.3589
5501408 0.5166 1.0114 0.8778 *1.3354
5501409 0.5277 0.9922 0.8758 *1.3100
0.0010 * extrapolated
0.8941 * extrapolated
0.6641 * extrapolated
0.0010
0.8941
0.6641
0.8941
0.8929
0.8925
0 .8915
0.8901
0.8601
0.7986
0.6641
0.1115
extrapolated
extrapolated
exN ý
*
lz
extrapolated
* extrapolated
0.9281
0.9263
0.9258
0.9244
0.9226
0.9211
0 .9195
0.9162
0.9116
0.9062
0.8995
0.8914
* extrapolated
0.7793
* extrapolated
0.9148
0.9255
0.9275
0.9277
0.9282
0.9295
0.9290
0.9269
*
extrapolated
5501410 0.5387 0.9745 0.8732 *1.2867 0.9242
5501411 0.5609 0.9373 0.8642 *1.2376 0.9146
0.9080
5501412 0.5719 0.9188 0.8579 *1.2131
5501413 0.5830 0.9003 0.8504 *1.1887 0.9000
*1.1636 0.8920
5501414 0.5941 0.8813 0.8428
5501415 0.7124 0.6786 0.7616 *0.8960 0.8061
*
relative pr eta pump 70% speed
*******.*********
5501501 0.0000 1.7500 0.0009
5501502 0.4613 1.4193 0.8507 *1.8740 0.9004
5501503 0.5447 1.2767 0.8723 *1.6857 0.9232
5501504 0.5587 1.2528 0.8759 *1.6541 0.9270
5501505 0.5726 1.2245 0.8781 *1.6168 0.9294
5501506 0.5866 1.1975 0.8785 *1.5811 0.9298
5501507 0.6006 1.1687 0.8798 *1.5430 0.9312
5501508 0.6145 1.1412 0.8796 *1.5067 0.9310
5501509 0.6285 1.1122 0.8778 *1.4684 0.9290
5501510 0.6425 1.0825 0.8753 *1.4292 0.9264
5501511 0.6565 1.0521 0.8716 *1.3891 0.9225
5501512 0.6704 1.0209 0.8684 *1.3479 0.9191
*1.3061 0.9128
5501513 0.6844 0.9892 0.8625
*1.2628 0.9030
5501514 0.6984 0.9564 0.8532
5501515 0.7124 0.9246 0.8413 *1.2208 0.8904
5501516 0.8358 0.6436 0.7359 *0.8498 0.7789
*
relative pr eta pump 80% speed
5501601 0.0000 2.1000 0.0009 ************9****
5501602 0.5447 1.7424 0.8600 *2.3005 0.9102
5501603 0.6638 1.4595 0.8764 *1.9270 0.9276
5501604 0.6810 1.4187 0.8788 *1.8732 0.9301
5501605 0.6982 1.3781 0.8799 *1.8195 0.9313
5501606 0.7154 1.3330 0.8805 *1.7600 0.9319
5501607 0.7326 1.2883 0.8804 *1.7010 0.9318
5501608 0.7498 1.2389 0.8780 *1.6357 0.9293
5501609 0.7670 1.1889 0.8745 *1 . 5697 0.9256
*1.5019 0.9231
5501610 0.7842 1.1375 0.8722
5501611 0.8014 1.0851 0.8648 *1.4327 0.9153
5501612 0.8186 1.0329 0.8541 *1.3638 0.9040
5501613 0.8358 0.9789 0.8440 *1.2925 0.8933
5501614 0.9702 0.5565 0.7651 *0.7347 0.8098
5501615 1.2390 -.2883 0.6073 *0.7347 0.8098
*
relative pr eta pump 90% speed
5501701 0.0000 2.4896 0.0009
5501702 0.6900 2.0358 0.8453
5501703 0.7000 2.0112 0.8489
5501704 0.7100 1.9859 0.8521
5501705 0.7200 1.9599 0.8550
5501706 0.7300 1.9334 0.8577
5501707 0.7400 1.9065 0.8600
5501708 0.7500 1.8792 0.8622
5501709 0.7600 1.8516 0.8643
5501710 0.7700 1.8239 0.8663
5501711 0.7800 1.7962 0.8683
5501712 0.7900 1.7685 0.8702
5501713 0.8000 1.7409 0.8722
5501714 0.8100 1.7136 0.8744
5501715 0.8200 1.6863 0.8765
5501716 0.8300 1.6585 0.8785
5501717 0.8400 1.6297 0.8800
* extrapolated
* extrapolated
* extrapolated
* extrapolated
extrapolated
extrapolated
5501718 0.8500 1.5993 0.8810
5501719 0.8600 1.5671 0.8815
5501720 0.8700 1.5331 0.8816
5501721 0.8800 1.4975 0.8812
5501722 0.8900 1.4607 0.8806
5501723 0.9000 1.4230 0.8795
5501724 0.9100 1.3846 0.8782
5501725 0.9200 1.3459 0.8766
5501726 0.9300 1.3070 0.8747
5501727 0.9400 1.2679 0.8724
5501728 0.9500 1.2286 0.8694
5501729 0.9600 1.1887 0.8655
5501730 0.9700 1.1480 0.8606
5501731 0.9800 1.1061 0.8543
5501732 0.9900 1.0633
0.8467
5501733 1.0000 1.0198 0.8381
5501734 1.0100 0.9761
0.8291
5501735 1.0200 0.9324 0.8199
5501736 1.0300 0.8885 0.8104
5501737 1.0400 0.8446 0.8007
5501738 1.0500 0.8006 0.7908
5501739 1.0600 0.7566 0.7808
5501740 1.0700 0.7125 0.7706
5501741 1.0800 0.6684 0.7604
5501742 1.0900 0.6242 0.7500
5501743 1.1000 0.5801 0.7396
5501744 1.1100 0.5359 0.7292
5501745 1.1200 0.4917 0.7188
5501746 1.1300 0.4476 0.7084
5501747 1.2812 1.6396 0.5571
*
relative pr eta pump 100% speed
5501801 0.0000 2.8896 0.0009
5501802 0.8100 2.4897 0.8507
5501803 0.8200 2.4586 0.8535
5501804 0.8300 2.4266 0.8561
5501805 0.8400 2.3939 0.8584
5501806 0.8500 2.3605 0.8605
5501807 0.8600 2.3264 0.8624
5501808 0.8700 2.2919 0.8642
5501809 0.8800 2.2570 0.8658
5501810 0.8900 2.2217 0.8673
5501811 0.9000 2.1862 0.8688
5501812 0.9100 2.1505 0.8701
5501813 0.9200 2.1147 0.8715
5501814 0.9300 2.0790 0.8728
5501815 0.9400 2.0434 0.8742
5501816 0.9500 2.0080 0.8756
5501817 0.9600 1.9728 0.8771
5501818 0.9700 1.9373 0.8786
5501819 0.9800 1.9003 0.8798
5501820 0.9900 1.8609 0.8808
5501821 1.0000 1.8188 0.8813
5501822 1.0100 1.7743 0.8814
5501823 1.0200 1.7279 0.8810
5501824 1.0300 1.6800 0.8801
5501825 1.0400 1.6310 0.8789
0.8775
5501826 1.0500 1.5813
5501827 1.0600 1.5308 0.8759
5501828 1.0700 1.4796 0.8741
5501829 1.0800 1.4273 0.8721
5501830 1.0900 1.3738 0.8697
5501831 1.1000 1.3187 0.8665
5501832 1.1100 1.2613 0.8618
5501833 1.1200 1.2013 0.8552
5501834 1.1300 1.1387 0.8467
5501835 1.2811 0.1272 0.6554
*
relative pr eta pump 110% speed
5501901 0.0000 3.2896 0.0009
5501902 0.9500 3.0082 0.8731
5501903 0.9600 2.9685 0.8753
5501904 0.9700 2.9277 0.8773
5501905 0.9800 2.8857 0.8790
5501906 0.9900 2.8425 0.8805
5501907 1.0000 2.7983 0.8818
5501908 1.0100 2.7529 0.8829
5501909 1.0200 2.7064 0.8837
5501910 1.0300 2.6589 0.8844
5501911 1.0400 2.6103 0.8848
5501912 1.0500 2.5607 0.8850
5501913 1.0600 2.5100 0.8851
5501914 1.0700 2.4584 0.8849
5501915 1.0800 2.4057 0.8846
5501916 1.0900 2.3521 0.8840
5501917 1.1000 2.2975 0.8833
5501918 1.1100 2.2420 0.8824
5501919 1.1200 2.1855 0.8813
5501920 1.1300 2.1280 0.8800
5501921 1.1400 2.0694 0.8785
5501922 1.1500 2.0097 0.8767
5501923 1.1600 1.9488 0.8748
5501924 1.1700 1.8866 0.8726
5501925 1.1800 1.8232 0.8701
5501926 1.1900 1.7586 0.8675
5501927 1.2000 1.6930 0.8646
5501928 1.2100 1.6265 0.8616
5501929 1.2200 1.5590 0.8584
5501930 1.2300 1.4908 0.8550
5501931 1.2400 1.4218 0.8515
5501932 1.2500 1.3522 0.8479
5501933 1.2600 1.2821 0.8442
5501934 1.2700 1.2115 0.8403
5501935 1.2800 1.1406 0.8365
5501936 1.3982 0.2778 0.7859
*
*
relative pr eta pump 120%
5502001 0.0000 3.5000 0.0009
5502002 0.6000 4.1500 0.2000
5502003 1.0748 3.4847 0.8746
5502004 1.3915 1.1814 0.8336
5502005 1.4100 0.6000 0.7000
speed
****************
* * extrapolated
* * extrapolated
*
*
relative pr eta pump 130% speed
5502101 0.0000 4.0000 0.0009 ****************
5502102 0.6000 5.0000 0.2000
5502103
5502104
5502105
1.2241
1.5319
1.5500
3.9712
1.2322
0.6000
0.8746
0.8336
0.7000
* * extrapolated
* * extrapolated
*
relative pr eta pump 140%
5502201 0.0000 4.3000 0.0009
5502202 0.6000 5.6000 0.2000
5502203 1.3734 4.4577 0.8746
5502204 1.6723 1.2830 0.8336
*
speed
****************
* * extrapolated
* * extrapolated
*
relative pr eta pump 150%
5502301 0.0000 4.7000 0.0009
5502302 0.6000 6.0000 0.2000
5502303 1.5227 4.9442 0.8746
5502304 1.8127 1.3338 0.8336
*
speed
****************
* * extrapolated
* * extrapolated
*
*5500500
*5500501 0.0 376.991
*5500502 1450. 376.991
$
*hydro
5600000
component name component type
snglvol
lpcout
*---------------------------------------------------------------------
$
*hydro
5600101
area
4.347
length
2.45
volume
0.0
*
*hydro
5600102
delta z
vert angle
horz angle
-2.45
0.0
-90.0
*
*hydro
5600103
hyd diam
roughness
0
0.0
0.0
fe
*
*hydro ebt pressure tempe
5600200 0 4357726. 1181832. 1181832. 1.
$
*hydro
5650000
component name component type
branch
lpc-ic
*-------------------------------------------------------------------
$
no. juns vel/flow
5650001 2
0
length
area
*hydro
2.45
4.347
5650101
*
volume
0.0
*
*hydro
5650102
vert angle
horz angle
-2.45
-90.0
0.0
delta z
*
*hydro
5650103
hyd diam
roughness
0
2.353
0.0
fe
*
*hydro ebt pressure tempe
5650200 0 4357863. 1181846. 1181846. 1.
area Kf Kr efvcahs
from to
*
0.0 0.0
5651101 560010000 565000000 0.0
0000000
5652101 565010000 570000000 0.0
0.0 0.0
*
velf
velg veli
5651201 12.9294 12.9294 0. * 319.2105
5652201 12.92918 12.92918 0. * 319.2105
*
hyd dia beta y-int slope
5651110 2.353 1.00 1.00 1.00
5652110 2.353 1.00 1.00 1.00
0000000
*
-**
*
570
5700000
Inter-cooler
intcool
pipe
*----------------------------------------------------------------------
*
no. vols
5700001 20
*
vol area
5700101 28.3 20
length
*
5700301 0.2365 20
*
volume
5700401 0.0 20
azim angle
*
5700501 0.0 20
*
incl angle
5700601 -90.0 20
*
roughness hyd dia
5700801 4.0e-3 9.924e-3 20
*
kf
kr
5700901 130.0 130.0 19.
*
pvbfe
5701001 00000 20
*
fvcahs
5701101 001000 19
*
ebt press temp
5701201 0 4358364. 1152563.
5701202 0 4356879. 1126299.
5701203 0 4355428. 1102891.
5701204 0 4354008. 1082014.
5701205 0 4352615. 1063381.
5701206 0 4351246. 1046744.
5701207 0 4349898. 1031881.
5701208 0 4348570. 1018596.
5701209 0 4347258. 1006716.
5701210 0 4345962. 996090.
5701211 0 4344678. 986582.
5701212 0 4343408. 978072.
5701213 0 4342148. 970453.
5701214 0 4340898. 963630.
5701215 0 4339656. 957520.
5701216 0 4338423. 952047.
5701217 0 4337196. 947144.
5701218 0 4335976. 942751.
5701219 0 4334760. 938816.
5701220 0 4333550. 935291.
1152563. 1. 0. 1
1126299. 1. 0. 2
1102891. 1. 0. 3
1082014. 1. 0. 4
1063381. 1. 0. 5
1046744. 1. 0. 6
1031881. 1. 0. 7
1018596. 1. 0. 8
1006716. 1. 0. 9
996090. 1. 0. 10
986582. 1. 0. 11
978072. 1. 0. 12
970453. 1. 0. 13
963630. 1. 0. 14
957520. 1. 0. 15
952047. 1. 0. 16
947144. 1. 0. 17
942751. 1. 0. 18
938816. 1. 0. 19
935291. 1. 0. 20
*
vel/flow
5701300 0
*
liquid vapor int-face
1 * 319.2105
5701301 1.936394 1.936394
5701302 1.892748 1.892748
2 * 319.2105
3 * 319.2105
5701303 1.853877 1.853877
5701304 1.81924 1.81924 0. 4 * 319.2105
5701305 1.78836 1.78836 0. 5 * 319.2105
5701306 1.76082 1.76082 0. 6 * 319.2105
5701307 1.736254 1.736254 0. 7 * 319.2105
5701308 1.71433
1.71433 0. 8 * 319.2105
5701309 1.694765 1.694765 0. 9 * 319.2105
1.6773 0.
10 * 319.2105
5701310 1.6773
5701311 1.661713 1.661713 0. 11 * 319.2105
12 * 319.2105
5701312 1.6478 1.6478 0.
635383 1.635383 0. 13 * 319.2105
5701313
5701314
624304 1.624304 0. 14 * 319.2105
614422 1.614422 0. 15 * 319.2105
5701315
* 319.2105
60561 1.60561 0.
5701316
* 319.2105
59776
1.59776 0.
5701317
590767 1.590767
18 * 319.2105
5701318
19 * 319.2105
584544 1.584544
5701319
*hydro jun diam beta intercept slope jun
5701401 9.924e-3 0.0 1.0 1.0 19
* 572
Junction - IC to HPC
*
*crdno
5720000
name
type
ic-hpcj
sngljun
*crdno from
to
5720101 570010000
area floss rloss
575000000 0.0 0.0
*crdno ctl flowf
5720201 0 89.372
flowg velj
89.372
0. * 319.2105
flag
0.0
-**
*
575
*crdno
5750000
Inlet pipe to high pressure compresser
name
type
ic-hpc
pipe
*
*crdno no.vols.
5750001
3
*crdno area
5750101 0.5
vol.no.
3
*
*crdno length
5750301 3.21
vol.no.
3
*
*crdno v-ang
5750601 90.0
vol.no.
*
*crdno rough dhy
vol.no.
3
5750801 0.5e-5 0.7979
*
*crdno
5750901
jun.no.
2
*
*crdno tlpvbf e
5751001 10000
vol.no.
3
*
*crdno
5751101
jefvcahs
jun.no.
2
0000000
*
*crdno
5751201
5751202
5751203
ebt pressure
0 4304494.
0 4303151.
0 4301978.
temp qual vol.no
932850. 932850. 1. 0.
932810. 932810. 1. 0.
932785. 932785. 1. 0.
1
2
3
*
*crdno i.c.
5751300 0
*
*crdno flowf flowg
velj
jun.no.
0.
1 * 319.2105
5751301 89.7534 89.7534
0.
2 * 319.2105
5751302 89.7788 89.7788
*
*crdno dhy
5751401 0.7979
jun. no
1.0 1.0
1.0
*
*
*
*
High pressure compressor
*
*--------------------------------------------------------------------
5800000
hpcmpr
cprssr
*--------------------------------------------------------*------*
*
*crdno nj
5800001 2
length
volume
*
area
*3500101 0.50
2.35
0.0
4.2
5800101 0.4762
0.0
*
azimrangle incl angle delta z pvbfe
90.0
5800102 0.00
4.2
00000
*
fromr jun area Kf
Kr fvc ahs
0.0 001000
5800108 575010000 0.0 0.0
*
to
jun area Kf
Kr fvc ahs
5800109 585000000 0.0 0.0
0.0 001000
*
hyd dia beta y-int slope
5800110 0.0000 0.00 1.00 1.00
5800111 0.0000 0.00 1.00 1.00
-------
*
ebt
5800200 3 7.21e6 378.05
vel/flow liquid vapor int-face
*
312.0 0.
0.0
5800201 1
312.0 0.
0.0
5800202 1
*
id mtr vel trip rvrs
0 350 0
*5800301 0 -1
-1 350 0
5800301 0 -1
rated vel sp ratio flow sound inertia density
*
5800302 376.991 1.000 319.21 692.04 2891.44 7.1263
mot coeff-tf2 coeff-tf0 coeff-tfl coeff-tf3
*
0.0
0.0
0.0
5800303 0.0 0.0
shaft trip
*
5800309 600 535
*
5800310 0. 1000. -0.00001
*----------------------------------------------------------------------
$
* performance curves based directly on mit calculations with
* extrapolations to boundary of adjacent curves; pump efficiencies
* performance data tables
Speed
nu
*
*crdno Rel Spd
*
-37.6991
3
5800910 -0.10
0.0 rad/s
*
4
5800911 0.00
150.7694
*
11
5800912 0.40
*
188.4955
14
5800913 0.50
226.1946
*
15
5800914 0.60
263.8937
*
16
5800915 0.70
301.5928
*
15
5800916 0.80
339.2919
*
47
5800917 0.90
376.9910
*
35
5800918 1.00
*
414.6901
36
5800919 1.10
452.3892
*
3
5800920 1.20
490.0883
*
3
5800921 1.30
527.7874
*
3
5800922 1.40
565.4865
*
3
5800923 1.50
pr
-10% speed
et
pump
a
*
relative
extrapolated
0. 9000 0.0009 *1.0000 0.0010
5801001 -0.1000
extrapolated
5801002 0.0000 0. 8500 0.0009 *0.9701 0.8941
extrapolated
5801003 0.4216 0. 6285 0.0009 *0.9619 0.6641
relative pr eta pump 0% speed
*
5801101 -0.1000 0.9300 0.0009
extrapolated
5801102 0.0000 1.0000 0.0009 *1.0000 0.0010
extrapolated
5801103 0.3736 0.7347 0.8448 *0.9701 0.8941
*0.9619
extrapolated
0.6641
5801104 0.4216 0.7285 0.6275
speed
relative pr eta pump 40%
*
5801201 -0.1000 0.9500 0.0009
******** *****•***
5801202 0.0000 1.1000 0.0009
5801203 0.3736 0.8171 0.8448 *1.0789 0.8941
5801204 0.3745 0.8164 0.8436 *1.0779 0.8929
5801205 0.3753 0.8158 0.8433 *1.0771 0.8925
5801206 0.3762 0.8149 0.8423 *1.0759 0.8915
5801207 0.3770 0.8141 0.8410 *1.0749 0.8901
5801208 0.3919 0.8006 0.8127 *1.0570 0.8601
5801209 0.4067 0.7868 0.7546 *1.0388 0.7986
5801210 0.4216 0.7728 0.6275 *1.0204 0.6641
5801211 0.4826 0.7157 0.1053 *0.9450 0.1115 * extrapolated
*
relative pr eta pump 50%
5801301 0.0000 1.3000 0.0009
5801302 0.3736 0.9769 0.8769
5801303 0.4026 0.9423 0.8752
5801304 0.4106 0.9328 0.8747
5801305 0.4186 0.9232 0.8734
5801306 0.4266 0.9139 0.8717
5801307 0.4346 0.9036 0.8703
5801308 0.4426 0.8940 0.8688
5801309 0.4506 0.8844 0.8657
5801310 0.4586 0.8742 0.8613
5801311 0.4666 0.8644 0.8562
5801312 0.4746 0.8543 0.8499
5801313 0.4826 0.8445 0.8422
5801314 0.5941 0.7087 0.7363
*
relative pr eta pump 60%
5801401 0.0000 1.5000 0.0009
5801402 0.4026 1.1765 0.8643
5801403 0.4613 1.0935 0.8745
5801404 0.4723 1.0779 0.8763
5801405 0.4834 1.0612 0.8765
5801406 0.4945 1.0447 0.8770
5801407 0.5055 1.0292 0.8782
5801408 0.5166 1.0114 0.8778
5801409 0.5277 0.9922 0.8758
5801410 0.5387 0.9745 0.8732
5801411 0.5609 0.9373 0.8642
5801412 0.5719 0.9188 0.8579
5801413 0.5830 0.9003 0.8504
5801414 0.5941 0.8813 0.8428
5801415 0.7124 0.6786 0.7616
*
relative pr eta pump 70%
5801501 0.0000 1.7500 0.0009
5801502 0.4613 1.4193 0.8507
5801503 0.5447 1.2767 0.8723
5801504 0.5587 1.2528 0.8759
5801505 0.5726 1.2245 0.8781
5801506 0.5866 1.1975 0.8785
5801507 0.6006 1.1687 0.8798
5801508 0.6145 1.1412 0.8796
5801509 0.6285 1.1122 0.8778
5801510 0.6425 1.0825 0.8753
5801511 0.6565 1.0521 0.8716
5801512 0.6704 1.0209 0.8684
5801513 0.6844 0.9892 0.8625
5801514 0.6984 0.9564 0.8532
5801515 0.7124 0.9246 0.8413
5801516 0.8358 0.6436 0.7359
*
relative pr eta pump 80%
5801601 0.0000 2.1000 0.0009
5801602 0.5447 1.7424 0.8600
5801603 0.6638 1.4595 0.8764
5801604 0.6810 1.4187 0.8788
5801605 0.6982 1.3781 0.8799
5801606 0.7154 1.3330 0.8805
5801607 0.7326 1.2883 0.8804
5801608 0.7498 1.2389 0.8780
speed
****************
*1.2898 0.9281
*1.2442 0.9263
*1.2316 0.9258
*1.2189 0.9244
*1.2066 0.9226
*1.1930 0.9211
*1.1804 0.9195
*1.1677 0.9162
*1.1542 0.9116
*1.1413 0.9062
*1.1279 0.8995
*1.1150 0.8914
*0.9357 0.7793
speed
****************
*1.5533 0.9148
*1.4438 0.9255
*1.4232 0.9275
*1.4011 0.9277
*1.3793 0.9282
*1.3589 0.9295
*1.3354 0.9290
*1.3100 0.9269
*1.2867 0.9242
*1.2376 0.9146
*1.2131 0.9080
*1.1887 0.9000
*1.1636 0.8920
*0.8960 0.8061
speed
****************
*1.8740 0.9004
*1.6857 0.9232
*1.6541 0.9270
*1.6168 0.9294
*1.5811 0.9298
*1.5430 0.9312
*1.5067 0.9310
*1.4684 0.9290
*1.4292 0.9264
*1.3891 0.9225
*1.3479 0.9191
*1.3061 0.9128
*1.2628 0.9030
*1.2208 0.8904
*0.8498 0.7789
speed
****************
*2.3005 0.9102
*1.9270 0.9276
*1.8732 0.9301
*1.8195 0.9313
*1.7600 0.9319
*1.7010 0.9318
*1.6357 0.9293
* extrapolated
* extrapolated
* extrapolated
* extrapolated
* extrapolated
* extrapolated
* extrapolated
5801609 0.7670 1.1889 0.8745 *1.5697
5801610 0.7842
1.1375 0.8722 *1.5019
1.0851 0.8648 *1.4327
5801611 0.8014
5801612 0.8186 1.0329 0.8541 *1.3638
5801613 0.8358
0.9789 0.8440 *1.2925
5801614 0.9702
0.5565 0.7651 *0.7347
5801615 1.2390
- .2883
0.6073 *0.7347
pr eta pump 90% speed
* relative
5801701 0.0000 2.5000 0.0009
5801702 0.6800 2.0462 0.8453
5801703 0.6900 2.0216 0.8489
5801704 0.7000 1.9963 0.8521
5801705 0.7100 1.9703 0.8550
5801706 0.7200 1.9438 0.8577
5801707 0.7300 1.9169
0.8600
5801708 0.7400 1.8896 0.8622
5801709 0.7500 1.8620 0.8643
5801710 0.7600 1.8343
0.8663
5801711 0.7700 1.8066
0.8683
5801712 0.7800 1.7789 0.8702
5801713 0.7900 1.7513
0.8722
5801714 0.8000
1.7240 0.8744
5801715 0.8100 1.6967
0.8765
5801716 0.8200
1.6689 0.8785
5801717 0.8300 1.6401 0.8800
5801718 0.8400
1.6097 0.8810
5801719 0.8500
1.5775 0.8815
5801720 0.8600 1.5435 0.8816
5801721
0.8700 1.5079 0.8812
5801722 0.8800
1.4711 0.8806
5801723 0.8900 1.4334 0.8795
5801724 0.9000
1.3950 0.8782
5801725 0.9100 1.3563 0.8766
5801726 0.9200 1.3174 0.8747
5801727 0.9300 1.2783 0.8724
5801728 0.9400 1.2390 0.8694
5801729 0.9500 1.1991 0.8655
5801730 0.9600 1.1584 0.8606
5801731 0.9700 1.1165 0.8543
0.8467
5801732 0.9800 1.0737
0.8381
5801733 0.9900 1.0302
5801734 1.0000 0.9865 0.8291
5801735 1.0100 0.9428 0.8199
5801736 1.0200 0.8989 0.8104
5801737 1.0300 0.8550 0.8007
5801738 1.0400 0.8110 0.7908
5801739 1.0500 0.7670 0.7808
5801740 1.0600
0.7229 0.7706
5801741 1.0700
0.6788 0.7604
5801742 1.0800 0.6346 0.7500
5801743 1.0900 0.5905 0.7396
5801744 1.1000 0.5463 0.7292
5801745 1.1100 0.5021 0.7188
5801746 1.1200 0.4580 0.7084
5801747 1.2712 1.6500 0.5571
*
relative pr eta pump 100% speed
5801801
0.0000 2.9000 0.0009
0.9256
0.9231
0.9153
0.9040
0.8933
0.8098 * extrapolated
0.8098 * extrapolated
5801802 0.8000 2.5001 0.8507
5801803 0.8100 2.4690 0.8535
5801804 0.8200 2.4370 0.8561
5801805 0.8300 2.4043 0.8584
5801806 0.8400 2.3709 0.8605
5801807 0.8500 2.3368 0.8624
5801808 0.8600 2.3023 0.8642
5801809 0.8700 2.2674 0.8658
5801810 0.8800 2.2321 0.8673
5801811 0.8900 2.1966 0.8688
5801812 0.9000 2.1609 0.8701
5801813 0.9100 2.1251 0.8715
5801814 0.9200 2.0894 0.8728
5801815 0.9300 2.0538 0.8742
5801816 0.9400 2.0184 0.8756
5801817 0.9500 1.9832 0.8771
5801818 0.9600 1.9477 0.8786
5801819 0.9700 1.9107 0.8798
5801820 0.9800 1.8713 0.8808
5801821 0.9900 1.8292 0.8813
5801822 1.0000 1.7847 0.8814
5801823 1.0100 1.7383 0.8810
5801824
1.0200 1.6904 0.8801
5801825 1.0300 1.6414 0.8789
5801826 1.0400 1.5917 0.8775
5801827 1.0500 1.5412 0.8759
5801828 1.0600 1.4900 0.8741
5801829 1.0700 1.4377 0.8721
5801830 1.0800 1.3842 0.8697
5801831 1.0900 1.3291 0.8665
5801832 1.1000 1.2717 0.8618
5801833 1.1100 1.2117 0.8552
5801834 1.1200 1.1491 0.8467
5801835 1.2711 0.1376 0.6554
*
rel ative pr eta pump 110% speed
5801901 0.0000 3.2896 0.0009
5801902 0.9400 3.0186 0.8731
5801903 0.9500 2.9789 0.8753
5801904 0.9600 2.9381 0.8773
5801905 0.9700 2.8961 0.8790
5801906 0.9800 2.8529 0.8805
5801907 0.9900 2.8087 0.8818
5801908 1.0000 2.7633 0.8829
5801909 1.0100 2.7168 0.8837
5801910 1.0200 2.6693 0.8844
5801911 1.0300 2.6207 0.8848
5801912 1.0400 2.5711 0.8850
5801913 1.0500 2.5204 0.8851
5801914 1.0600 2.4688 0.8849
5801915 1.0700 2.4161 0.8846
5801916 1.0800 2.3625 0.8840
5801917 1.0900 2.3079 0.8833
5801918 1.1000 2.2524 0.8824
5801919 1.1100 2.1959 0.8813
5801920 1.1200 2.1384 0.8800
5801921 1.1300 2.0798 0.8785
5801922 1.1400 2.0201 0.8767
5801923
5801924
5801925
5801926
5801927
5801928
5801929
5801930
5801931
5801932
5801933
5801934
5801935
5801936
1.1500
1.1600
1.1700
1.1800
1.1900
1.2000
1.2100
1.2200
1.2300
1.2400
1.2500
1.2600
1.2700
1.3882
1.9592
1.8970
1.8336
1.7690
1.7034
1.6369
1.5694
1.5012
1.4322
1.3626
1.2925
1.2219
1.1510
0.2882
0.8748
0.8726
0.8701
0.8675
0.8646
0.8616
0.8584
0.8550
0.8515
0.8479
0.8442
0.8403
0.8365
0.7859
*
relative pr eta pump 120%
5802001 0.0000 3.5000 0.0009
5802002 1.0748 3.4847 0.8746
5802003 1.3915 1.1814 0.8336
speed
*
relative pr eta pump 130%
5802101 0.0000 4.0000 0.0009
5802102 1.2241 3.9712 0.8746
5802103 1.5319 1.2322 0.8336
speed
*************lated
** ** extrapolated
extrapolated
********extrapolated
** ** extrapolated
extrapolated
*
relative pr eta pump 140% speed
*e*************
5802201 0.0000 4.3000 0.0009
5802202 1.3734 4.4577 0.8746 * * extrapolated
5802203 1.6723 1.2830 0.8336 * * extrapolated
*
*
relative pr eta pump 150% speed
5802301 0.0000 4.7000 0.0009 ****W************
5802302 1.5227 4.9442 0.8746 * * extrapolated
5802303
1.8127 1.3338 0.8336 * * extrapolated
*5800500
*5800501 0.0 376.991
*5800502 1450. 376.991
$
*hydro
5850000
component name component type
hpout
snglvol
*---------------------------------------------------------------------
*hydro
5850101
*hydro
5850102
area
0.5
length
1.0
volume
0.0
horz angle
vert angle
0.0
0.0
0.0
delta z
*
*hydro
5850103
hyd diam
roughness
0.0
0.0
*hydro ebt pressure tempe
5850200 0 7210130. 1173657. 1173657. 1.
$
*hydro
5870000
component name component type
hp-rc
branch
*---------------------------------------------------------------
*
no. juns vel/flow
5870001 2
0
*hydro
area
length
1.0
0.5
5870101
*hydro
5870102
volume
0.0
horz angle
vert angle
0.0
0.0
0.0
delta z
*
*hydro
5870103
roughness
hyd diam
0.7979
0.0
*hydro ebt pressure tempe
5870200 0 7209954. 1173663. 1173663. 1.
*
from to
area Kf Kr efvcahs
0.0 0.0
5871101 585010000 587000000 0.5
0.0 0.0
5872101 587010000 590000000 0.0
*
velf
velg veli
5871201 67.6061 67.6061 0. * 319.2105
5872201 67.6074 67.6074 0. * 319.2104
*
hyd dia beta y-int slope
5871110 0.7979 1.00 1.00 1.00
5872110 0.7979 1.00 1.00 1.00
0000000
0000000
*
$
5900000
rc-hp
pipe
*---------------------------------------------------------
*
no. vols
5900001
*
-----
30
vol area
5900101 7.32 30
*
length
5900301 0.09384
*
volume
5900401 0.0 30
*
azim angle
5900501 0.0 30
*
incl angle
5900601 90.0 30
roughness hyd dia
*
5900801 1.5-4 1.067e-3 30
*
kf
kr
5900901 14.0
14.0 29
*
pvbfe
5901001 00000 30
*
fvcahs
5901101 001000 29
*
ebt
5901201 0 7231182. 1212588.
5901202 0 7229406. 1250813.
5901203 0 7227566. 1289093.
5901204 0 7225664. 1327414.
1212588.
1250813.
1289093.
1327414.
1.
1.
1.
1.
0.
0.
0.
0.
1
2
3
4
5901205
7223700. 1365766. 1365766.
7221672. 1404137. 1404137.
5901206
7219580. 1442517. 1442517.
5901207
7217424. 1480896. 1480896.
5901208
5901209
7215203. 1519265. 1519265.
5901210
7212918. 1557615. 1557615.
5901211
7210568. 1595938. 1595938.
7208154. 1634226. 1634226.
5901212
7205674. 1672471. 1672471.
5901213
7203128. 1710667. 1710667.
5901214
7200516. 1748806. 1748806.
5901215
7197838. 1786883. 1786883.
5901216
5901217
7195095. 1824891. 1824891.
7192285. 1862826. 1862826.
5901218
5901219
7189408. 1900682. 1900682.
5901220
7186466. 1938455. 1938455.
7183456. 1976141. 1976141.
5901221
5901222
7180379. 2013735. 2013735.
5901223
7177236. 2051233. 2051233.
7174025. 2088632. 2088632.
5901224
7170748. 2125927. 2125927.
5901225
7167402. 2163116. 2163116.
5901226
7163990. 2200194. 2200194.
5901227
7160510. 2237160. 2237160.
5901228
7156964. 2274011. 2274011.
5901229
7153350. 2310746. 2310746.
5901230
*
vel/flow
5901300 0
*
liquid vapor int-face
5901301 4.76433 4.76433 0. 1 * 319.2104
5901302 4.91561 4.91561 0. 2 * 319.2104
5901303 5.06717 5.06717 0. 3 * 319.2104
5901304 5.21897 5.21897 0. 4 * 319.2104
5901305 5.37095 5.37095 0. 5 * 319.2104
5901306 5.52307 5.52307 0. 6 * 319.2104
7 * 319.2105
5901307 5.6753 5.6753 0.
5901308 5.82761 5.82761 0. 8 * 319.2105
5901309 5.97995 5.97995 0. 9 * 319.2105
10 * 319.2105
5901310 6.1323 6.1323 0.
5901311 6.28462 6.28462 0. 11 * 319.2105
12 * 319.2105
5901312 6.4369 6.4369 0.
5901313 6.58909 6.58909 0. 13 * 319.2105
5901314 6.74117 6.74117 0. 14 * 319.2105
5901315 6.89313 6.89313 0. 15 * 319.2105
5901316 7.04494 7.04494 0. 16 * 319.2105
5901317 7.19658 7.19658 0. 17 * 319.2105
5901318 7.34803 7.34803 0. 18 * 319.2105
5901319 7.49927 7.49927 0. 19 * 319.2105
20 * 319.2105
5901320 7.6503 7.6503 0.
5901321 7.80109 7.80109 0. 21 * 319.2105
5901322 7.95163 7.95163 0. 22 * 319.2105
8.10192 0. 23 * 319.2105
5901323 8.10192
5901324 8.25193 8.25193 0. 24 * 319.2105
5901325 8.40165 8.40165 0. 25 * 319.2105
5901326 8.55108 8.55108 0. 26 * 319.2105
27 * 319.2105
8.7002 8.7002 0.
5901327
5901328 8.84901 8.84901 0. 28 * 319.2105
5901329 8.9975 8.9975 0.
29 * 319.2105
*hydro jun diam beta intercept slope jun
5901401 1.067e-3 0.0 1.0 1.0 29
*
Name Valve
5910000 bypass tmdpjun
*
from
to
5910101 590010000 592000000
*
cntrl trp
5910200 1
1005
5910201 -0.* 0. 0. 0.
5910201 -0. 0. 0. 0.
0. 0. 10. 0.
5910202
**
area
0.00
j-flag
0000000
*
*---------------------------------------------------------
*crdno
5920000
name
cprbp2
type
tmdpvol
*
*crdno
5920101
area lngth vol
78. .9104 0 0
h-a v-ang delz
0. .0 0 1.5
rgh dhy
00010
*
*crdno ebt
5920200 3
*crdno time
5920201 0.0
press temp
3e5 740.
*
Name Valve
5930000 RCC1g valve
*
from
to
area
kforw kbackw j-flag
5930101 590010000 595000000 0.00 0. 0. 0000000
*
cntrl w/v.liq w/v.vap w/v.int
5930201 1 0.
319.2105 0.0
*
valve-type
5930300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
5930301 1004
**
*
$
*crdno name type
5950000 rcoutj branch
5950001 1
0
5950101 0.5
2.8152 0.0
5950102 0.0
-90.0 -2.8152
5950103 0.0 0.7979
11000
5950200 0
7109896. 2307731. 2307731. 1.
*crdno from
to
area floss rloss flag
*5951101 590010000 595000000 0.0 0.0 0.0 000000
5951101 595010000 597000000 0.0 0.0 0.0 000000
*crdno flowf flowg velj
*5951201 133.8927 133.8927 0. * 319.2105
5951201 134.1854 134.1854 0. * 319.2105
*
*
*
pvbfe
*
597
Hot Duct volume
*
* crdno
name
type
cldduct
pipe
5970000
*
*crdno no.vols.
5970001
4
*
*crdno area
5970101 1.885
vol
.no.
4
*
*crdno length
5970301 1.85
vol.no.
4
*
*crdno v-ang
5970601 0.0
vol
4
.no.
*
*crdno rough
5970801 0.
dhy
0.6
vol.no.
4
*
*crdno
5970901
ff
0.
rf
0.
jun.no.
3
*
*crdno tlpvbfe
5971001 10010
vol.no.
4
*
*crdno
5971101
jefvcahs
jun.no.
3
0000000
*
*crdno
5971201
5971202
5971203
5971204
ebt pressure
0 7149064.
0 7149072.
0 7149072.
0 7149072.
temp qual vol.no.
2310600. 2310600. 1.
2310600. 2310600. 1.
2310600. 2310600. 1.
2310600. 2310600. 1.
0.
0.
0.
0.
1
2
3
4
*
*crdno i.c.
5971300 0
*
*crdno flowf flowg
velj
jun.no.
5971301 35.525 35.525
0.
1 * 319.2105
5971302 35.525 35.525
0.
2 * 319.2105
5971303 35.525 35.525
0.
3 * 319.2105
*
*crdno dhy
5971401 0.6
1.0
jun. no
1.0 1.0
3
*
*====
===
====
==-
=-=
====
===
==-
=-==
===
===-
=-
=
===
==-=-
===
===
====
===
===
====
===
====
=-
=
-==
====
==
===
*
*
**
Bypass Line
*
*====
**
*
===
=-==
===
===
4040000
4040001
4040101
4040102
4040103
4040200
4041101
4041110
4041201
bypvo21 branch
0
1
0.1039 9.144 0.0
0.0
0.0
0.0
3.048-7 0.0 11000
0
7231534. 1175566. 1175566. 1.
587010002 404010001 0.0 0.0 0.0 000000
1.0 1.0
0.0 0.0
-6.90005-7 -6.90005-7 0. * -6.76943-7
4050000
4050101
4050102
4050103
4050201
4050300
4050301
4050302
bypsvl2 valve
404010002 406010001
000100
0.5
0.5
1.0
1.0
1.0
0. 0. * 0.
1
0.
mtrvlv
1.0
481
482
0.0
0
4060000
4060001
4060101
4060102
4060103
4060200
4061101
4061110
4061201
bypvl22 branch
1
0
0.1039 9.144 0.0
0.0
90.0 4.2
3.048-7 0.0 11000
0
3049666. 2494429. 2494429. 1.
406010002 515010001 0.0 0.0 0.0 000000
0.0 0.0
1.0 1.0
-1.244698-9 -1.244698-9 0. * - 2.31131-10
0.1039
*-----------------------------------*
*
**
*-
Source of cooling water for precooler
Source of cooling water for precooler
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
- ==
-
- ===
-
- ===
-
**
*
131 Water Source
*
*crdno
1310000
name
h2_cd
type
tmdpvol
*
*crdno
1310101
area lngth vol
78.
.9104 0 0
*crdno ebt
1310200 3
*crdno time
1310201 0.0
h-a v-ang delz
0. .0 0 1.5
press temp
0.84e6 293.15
rgh dhy
00010
pvbfe
- ===-
- ===-
-- ===
*crdno
1320000
name
hecdj
type
sngljun
*crdno from
to
1320101 131000000
area floss rloss
133000000 0.0 0.
flag
0.
*
*crdno ctl flowf flowg velj
1320201 0 1.490186 1.520952 0.
* 1253.5
*
-*m
1330000
prech2o
pipe
*-------------------------------------------------------------------
*
no. vols
1330001 20
*
vol area
1330101 0.8423 20
*
length
1330301 0.2365 20
*
volume
1330401 0.0 20
azim angle
*
1330501 0.0 20
*
incl angle
1330601 90.0 20
*
roughness hyd dia
1330801 0.0 2.0e-3 20
kr
*
kf
1330901 13.7 13.7 19
*
pvbfe
1331001 00000 20
*
fvcahs
1331101 001000 19
temp
*
ebt press
84988. 2576484. 0. 0. 1
834479.
1331201
86349.6 2575659.
811195.
1331202
87917.5 2574782.
787915.
1331203
89721.8 2573852.
764650.
1331204
91796.9 2572900.
741402.
1331205
94182.4 2571848.
718173.
1331206
96923.8 2570730.
694965.
1331207
100073.6 2569583.
671782.
1331208
103692.4 2568406.
648627.
1331209
107850. 2567196.
625502.
1331210
112627. 2565952.
602412.
1331211
118117. 2564672.
579360.
1331212
124428.4 2563352.
556350.
1331213
131686.8 2561992.
533387.
1331214
140038.7 2560586.
510475.
1331215
149655. 2559134.
487618.
1331216
160735.3 2557629.
464821.
1331217
173512.7 2556068.
442088.
1331218
188262. 2554324.
1331219
419421.
205304.8 2552454.
396824.
1331220
*
vel/flow
1331300 0
100
*
liquid vapor int-face
1331301 1.490278 1.538892 0. 1 * 1253.5
1331302 1.490396 1.559857 0. 2 * 1253.5
1331303 1.490533 1.58196 0. 3 * 1253.5
1331304 1.49069 1.60508 0. 4 * 1253.5
1331305 1.490873 1.62915 0. 5 * 1253.5
1331306 1.491085 1.654127 0. 6 * 1253.5
1331307 1.491332 1.679986 0. 7 * 1253.5
1331308 1.491623 1.706704 0. 8 * 1253.5
1331309 1.491964 1.734265 0. 9 * 1253.5
1331310 1.492368 1.762648 0. 10 * 1253.5
1331311 1.492847 1.791832 0. 11 * 1253.5
1331312 1.49342 1.821788 0. 12 * 1253.5
1331313 1.494103 1.85248 0. 13 * 1253.5
1331314 1.494926 1.883866 0. 14 * 1253.5
1331315 1.49592 1.915887 0. 15 * 1253.5
1331316 1.497126 1.92571 0. 16 * 1253.5
1331317 1.498594 1.92763 0. 17 * 1253.5
1331318 1.50039 1.929976 0. 18 * 1253.5
1331319 1.502596 1.93286 0. 19 * 1253.5
*hydro jun diam beta intercept slope jun
1331401 2.0e-3 0.0 1.0 1.0 19
$
*
*
134
Junction
-
cooling outlet
*
1340000
coreij tmdpjun
*crdno from
to
area jefvcahs
1340101 133010000 135000000 0.0
1340200 1
1340201 0.0 1.2535e3 0.0 0.0
*135
*
000000
Water Sink
*
*
135 Water Sink
*crdno
1350000
name
hi_cold
type
tmdpvol
*
*crdno
1350101
area lngth vol
78. .9104 0 0
h-a v-ang delz
0. .0 0 1.5
*
*crdno ebt
1350200 3
*crdno time
1350201 0.0
press
0.54e6
temp
325.15
***
Source of cooling water for intercooler
*141
Water Source
*
* 141 Water Source
*
rgh dhy
00010
pvbfe
*crdno
1410000
*crdno
1410101
name
h2ccd
type
tmdpvol
area lngth vol
78.
.9104 0 0
h-a v-ang delz
0. .0 0 1.5
rgh dhy
00010
pvbfe
*
*crdno ebt
1410200 3
*crdno time
1410201 0.0
press temp
0.84e6
293.15
*
*
*--
*crdno
1420000
name
hcdj
type
sngljun
*
*crdno from
to
1420101 141000000
area floss rloss
143000000 0.0 0.
flag
0.
100
*
*crdno ctl flowf flowg velj
1420201 0 1.62224 1.65259 0. * 985.
*
1430000
intch2o
pipe
*--------------------------------------------------------- ------------
*
no. vols
1430001 20
*
vol area
1430101 0.608 20
*
length
1430301 0.2365 20
*
volume
1430401 0.0 20
*
azim angle
1430501 0.0 20
*
incl angle
1430601 90.0 20
*
roughness hyd dia
1430801 0.0 2.0e-3 20
kr
kf
*
1430901 12.
12.
19
*
pvbfe
1431001 00000 20
*
fvcahs
1431101 001000 19
*
ebt press
temp
85647.2 2576458. 0. 0. 1
1431201 0 833749.
87706.5 2575581. 0. 0. 2
1431202 0 809012.
90010.2 2574638. 0. 0. 3
1431203
0 784296.
92586.7 2573647. 0. 0. 4
1431204 0 759605.
95467.7 2572631. 0. 0. 5
1431205 0 734941.
98689. 2571472. 0. 0. 6
1431206 0 710307.
102290.8 2570276. 0. 0. 7
1431207 0 685704.
106318. 2569046. 0. 0. 8
1431208 0 661137.
110821.3 2567782. 0. 0. 9
1431209 0 636608.
1431210 0 612120.
115857
2566480.
1431211 0 587677.
121490
2565138.
1431212 0 563283.
127793
2563754.
1431213 0 538940.
134846
2562325.
1431214 0 514652.
142742
2560846.
1431215 0 490423.
151586
2559314.
1431216 0 466255.
161494
2557725.
1431217 0 442152.
172602
2556073.
1431218 0 418115.5 185061
2554218.
1431219 0 394148.
199045
2552214.
1431220 0 370250.
214750
2550009.
*
vel/flow
1431300 0
*
liquid vapor int-face
1431301 1.622396 1.67498 0. 1 * 985.
1431302 1.622586 1.69937 0. 2 * 985.
1431303 1.6228 1.725116 0. 3 * 985.
1431304 1.623046 1.752073 0. 4 * 985.
1431305 1.623326 1.78016 0. 5 * 985.
1431306 1.623645 1.809332 0. 6 * 985.
1431307 1.624012 1.839554 0. 7 * 985.
1431308 1.624434 1.8708 0. 8 * 985.
1431309 1.62492 1.903052 0. 9 * 985.
1431310 1.625485 1.93628 0. 10 * 985.
1431311 1.62614 1.970453 0. 11 * 985.
1431312 1.626903 2.00553 0. 12 * 985.
1431313 1.627794 2.04146 0. 13 * 985.
1431314 1.628838 2.07817 0. 14 * 985.
1431315 1.630063 2.09947 0. 15 * 985.
1431316 1.631506 2.101357 0. 16 * 985.
1431317 1.633208 2.103583 0. 17 * 985.
1431318 1.635222 2.106216 0. 18 * 985.
1431319 1.63761 2.10934 0. 19 * 985.
*hydro jun diam beta intercept slope jun
1431401 2.0e-3 0.0 1.0 1.0 19
*-
-
-
-
* 144
-
-
-
-
-
-
-
-
-
-
-
-
-
-
*145
*
-
-
-
-
-
-
==
-
- === -
- ===-
Junction - cooling outlet
1440000
coreij tmdpjun
*crdno from
to
area jefvcahs
1440101 143010000 145000000 0.0
1440200 1
1440201 0.0 0.985e3 0.0 0.0
*
*
-
000000
Water Sink
145 Water Sink
*
*crdno
1450000
name
hi_cold
type
tmdpvol
*
*crdno
1450101
*
area lngth vol
78. .9104 0 0
h-a v-ang delz
0. .0 0 1.5
rgh dhy
00010
pvbfe
- ===
- ===-
--
==
*crdno ebt
1450200 3
*crdno time
1450201 0.0
*
press
0.54e6
temp
325.15
PCU Model Configuration-Hot Side
*
*---------------------------------------------------------
*
PCU Junction: Reactor Outlet Plenum to PCU Hot Duct
*---------------------------------------------------------
*
name
junction
0820000 RPV-Hdct valve
*
from
to
area kforw kbackw j-flag
0820101 300010000 504000000 1.606 8.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
0820201 0 62.7588 62.7588 0. * 319.2105
*
valve-type
0820300 mtrvlv
trip# w/v.liq w/v.vap w/v.int
*
1003
0.0167
1.0
0820301 527
00000200
*
**
Name Valve
5030000 cprbp2 valve
*
from
to
area
kforw kbackw j-flag
5030101 504010000 500000000 0.00 0. 0. 0000000
*
cntrl w/v.liq w/v.vap w/v.int
5030201 1 0.
0. 0.0
*
valve-type
5030300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
5030301 1004
*
*--------------------------------------------------------*
*---------------------------------------------------------
*crdno name type
5040000 contnmt snglvol
*crdno area length vol h-a v-ang delz rgh dhy pvbfe
*
5040101 1.606 0.1 0 0 0. .0 0. 0. 00010
*crdno ebt press temp.
5040200 0 7001960. 3442779. 3442779. 1. 0.
*
*---------------------------------------------------------
*
Single Volume: Guard Containment
*---------------------------------------------------------
*crdno name type
0700000 contnmt snglvol
*crdno area length vol h-a v-ang delz rgh dhy
0700101 283.0 10.15 0 0 0. .0 0. 0. 00010
*crdno ebt press temp.
0700200 3 1.0e5 303.15
*-----------------------------------------------
pvbfe
* 283x66.15
*
Single Volume: nossle
*---------------------------------------------------------
*crdno name type
*0630000 contnmt snglvol
*crdno area length vol h-a v-ang delz rgh dhy pvbfe
*0630101 0.05 0.01 0 0 0. .0 0. 0. 00010
*
*crdno ebt press temp.
*0630200 3 1.0e5 303.15
*---------------------------------------------------------
*
Single Junction: nossle
*---------------------------------------------------------
**
name
junction
*0640000 tocont sngljun
*
from
to
area kforw kbackw j-flag
*0640101 063010000 070000000 0.0 0.23 0.23
*
cntrl w/v.liq w/v.vap w/v.int
*0640201 0 0. 0. 0. *
0000000
*---------------------------------------------------------
*
Valve: PCU to Guard Containment
*---------------------------------------------------------
**
Name Valve
0620000 PCU-GC valve
kforw kbackw j-flag
*
from
to
area
0620101 597010000 070000000 0.0005 1.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
0620201 1 0.
0.0 0.0
*
valve-type
0620300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
0620301 522 *CLOSE until 50 secs
0000000
*
*----------------------------------------------------
*
083
Junction between PCU and RPV inlet (cold duct)
*----------------------------------------------------
*0830000 pcuhot tmdpjun
*crdno from
to
area jefvcahs
*0830101 597010000 670000000 1.885 000000
*0830200 1 522
*0830201 -1.0 0.0 0.0 0.0
*0830202 0.0 0.0 324.57 0.0
*0830203 1.0 0.0 324.57 0.0
*0830204 50.0 0.0 0.0 0.0
*Note times above are trip tim + given time
*
*
*---------------------------------------------------------
*
PCU Junction: PCU Cold Duct to RPV Downcomer
*---------------------------------------------------------
*
name
junction
9650000 InC-InHP sngljun
*
from
to
area kforw kbackw j-flag
9650101 597010000 670000000 0.0 0.0 0.0
*
cntrl w/v.liq w/v.vap w/v.int
9650201 0 35.525 35.525 0. * 319.2105
0000000
*
*---------------------------------------------------------
*
PCU Junction: PCU Cold Duct to RPV Downcomer
*-----------------------------------------
--
junction
*
name
9660000 InC-InHP sngljun
to
area kforw kbackw j-flag
*
from
9660101 597010000 800000000 0.0 0.0 0.0
*
cntrl w/v.liq w/v.vap w/v.int
9660201 0 35.525 35.525 0. * 319.2105
--
------
0000000
*
*
*
Passive DHR DECAY HEAT REMOVAL SYSTEM 1
*
*
*---------------------------------------------------------
*
Junction: Reactor Outlet Plenum to Passive DHR System Duct
*---------------------------------------------------------
**
name
junction
6050000 opl-hd sngljun
*
from
to
area kforw kbackw j-flag
6050101 300010000 610000000 0.0 0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6050201 0 -1.298463-7 -1.298463-7 0. * -4.31083-7
*---------------------------------------------------------
*
Passive DHR Hot Duct
1x50% loop
*---------------------------------------------------------
*
name pipe/annulus
6100000 hp-hotd pipe
*
number of volumes
6100001 5
area no of vol
*
6100101 2.0774 5
*
length no of vol
6100301 3.8
5
*
volume no of vol
6100401 0.0
5
*
azi ang no of vol
5
6100501 90.
*
ver ang no of vol
5
6100601 90.
elev. no of vol
*
5
6100701 3.0
*
rough dhydr. no of vol
6100801 4.5e-5 1.6264 5
*
kforw kbackw no of jun
4
6100901 0.0875 0.0875
*
v-flag no of vol
6101001 00000 5
*
j-flag
no of jun
6101101 000000 4
*
cntrl pressure temperature * * * no of vol
7058062. 3418188. 3418188. 1. 0. 1
6101201 0
7.058+6 3403438. 3403438. 1. 0. 2
6101202 0
7057949. 3400732. 3400732. 1. 0. 3
6101203 0
7057892. 3401820. 3401820. 1. 0. 4
6101204 0
6101205 0
7057836. 3411673. 3411673. 1. 0. 5
*
cntrl
6101300 0
*
w/v.liq w/v.vap w/v.int no of jun
6101301 -1.256998-7 -1.256998-7 0. 1 * -4.19126-7
6101302 -1.221132-7 -1.221132-7 0. 2 * -4.07489-7
6101303 -1.18709-7 -1.18709-7 0.
3 * -3.96001-7
6101304 -1.156956-7 -1.156956-7 0. 4 * -3.848304-7
*
*---------------------------------------------------------
*
Junction: HP Hot Duct to HX POD Inlet
*---------------------------------------------------------
*
name
junction
6150000 hd-hxpin sngljun
*
from
to
area kforw kbackw j-flag
6150101 610010000 620000000 0.0 0.75 0.75 0000001
*
cntrl w/v.liq w/v.vap w/v.int
6150201 0 -1.158115-7 -1.158115-7 0. * -3.76676-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger POD Inlet
*---------------------------------------------------------
*
name
volume
6200000 hp-hxpin snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6200101 5.4
4.5 0.0 90. 90. 4.5 4.5e-5 1.636 000000 $ 1
*
cntrl press
temp
6200200 0
7057738. 3488909. 3488909. 1.
*---------------------------------------------------------
*
Junction: Passive DHR HX POD Inlet to Heat Exchanger Inlet
*---------------------------------------------------------
*
name
junction
6250000 ihx-hxp sngljun
*
from
to
area kforw kbackw j-flag
6250101 620010000 626000000 0.0
0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6250201 0 -3.62896-8 -3.62896-8 0. * -2.489533-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Inlet
*---------------------------------------------------------
*
name
volume
6260000 hp-hxin snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6260101 2.1276 1.0 0.0 -90.
-90.
-0.5 4.5e-5 0.15 000000
*
cntrl press temp
6260200 0
7057678. 3388292. 3388292. 1.
*---------------------------------------------------------
*
Junction: Passive DHR HX Inlet to Heat Exchanger
*---------------------------------------------------------
*
name
junction
6270000 ihx-hx sngljun
*
from
to
area kforw kbackw j-flag
6270101 626010000 650000000 0.0 0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6270201 0 -2.086635-8 -2.086635-8 0. * -2.680236-7
*
$ 1
*
Passive DHR Heat Exchanger
*---------------------------------------------------------
*
name pipe/annulus
6500000 hp-hx pipe
*
number of volumes
6500001 5
*
area no of vol
6500101 2.1856 5
*
length no of vol
6500301 0.060 5
*
volume no of vol
6500401 0.0
5
azi ang no of vol
*
6500501 -90.
5
*
ver ang no of vol
6500601 -90.
5
elev. no of vol
*
6500701 -0.060 5
*
rough dhydr. no of vol
6500801 1.e-5 3.055e-3 5
*
kforw kbackw no of jun
6500901 0.0
0.0
4
*
v-flag no of vol
6501001 00000 5
*
j-flag no of jun
6501101 000000 4
*
cntrl pressure temperature * * * no of vol
6501201 0
7057689. 932251. 932251. 1. 0. 1
6501202 0
7057696. 932245. 932245. 1. 0. 2
6501203 0
7057702. 932240. 932240. 1. 0. 3
6501204 0
7057710. 932236. 932236. 1. 0. 4
6501205 0
7057716. 932233. 932233. 1. 0. 5
*
cntrl
6501300 0
*
w/v.liq w/v.vap w/v.int no of jun
6501301 -2.098683-8 -2.098683-8 0. 1 * -2.69573-7
6501302 -2.108813-8 -2.108813-8 0. 2 * -2.708757-7
6501303 -2.11641-8 -2.11641-8 0. 3 * -2.71853-7
6501304 -2.12116-8 -2.12116-8 0. 4 * -2.724644-7
*---------------------------------------------------------
*
Junction: Passive DHR Heat Exchanger to HX Outlet
*---------------------------------------------------------
*
name
junction
6550000 hx-ohx sngljun
*
from
to
area kforw kbackw j-flag
6550101 650010000 660000000 0.0 0.50 0.50 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6550201 0 -4.34546-8 -4.34546-8 0. * -2.737685-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Outlet Plenum
*---------------------------------------------------------
*
name
volume
6600000 hp-outpl snglvol
length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
area
-90.
-0.2 4.5e-5 0.15 000000
6600101 2.1276 1.0 0.0 -90.
*
cntrl press
temp
6600200 0
7057726. 1896749. 1896749. 1.
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet to Downcomer
*---------------------------------------------------------
*
name
junction
6610000 hp-ohx sngljun
*
from
to
area kforw kbackw j-flag
6610101 660010000 662000000 0.0 1.0 1.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6610201 0 -2.273712-8 -2.273712-8 0. * -2.254984-7
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Outlet Pod
*---------------------------------------------------------
*
name
volume
6620000 hp-outpp snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6620101 10.995 1.0 0.0 -90. -90.
-1.0 4.5e-5 2.026 000000
*
cntrl press
temp
6620200 0
7057754. 2344926. 2344926. 1.
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet Pod
*---------------------------------------------------------
*
name
junction
6630000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
6630101 662010000 664000000 0.0 0.0 0.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6630201 0 -4.49314-9 -4.49314-9 0. * -1.282388-7
*
*---------------------------------------------------------
*
Passive DHR
BLOWER volume
*---------------------------------------------------------
*
name
volume
6640000 hp-outpb snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6640101 6.1576 3.0 0.0 -90.
-90. -3.0 4.5e-5 1.4 000000
*
cntrl press
temp
6640200 0
7057845. 2358240. 2358240. 1.
*
*
name
junction
6920000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
6920101 664010000 690000000 0.0
0.0 0.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6920201 0 -4.67222-9 -4.67222-9 0. * -1.88798-7
*---------------------------------------------------------
*
name
volume
6900000 hp-outpc snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6900101 6.1576 0.5 0.0 -90. 0. 0.0 0. 1.4 000000
*
cntrl press
temp
6900200 0
7057892. 1666776. 1666776. 1.
*
*-------------------------------------------
$
*
name
junction
6650000 hp-blow valve
*
from
to
area kforw kbackw j-flag
6650101 690010000 698000000 6.1576 13.46 13.46
cntrl w/v.liq w/v.vap w/v.int
*
6650201 0 0.
0. 0. * 0.
valve-type
*
6650300 mtrvlv
*
trip# w/v.liq w/v.vap w/v.int
6650301 539
541
0.025
0.0
00000200
*-------------------------------------------------------------
**
Name Valve
6870000 leakl tmdpjun
*
from
to
6870101 698000000 690010000
*
cntrl trp
541
6870200 1
6870201 -0.1 0. 0. 0.
6870201 -0. 0. 0.15 0.
0. 0. 0.15 0.
6870202
area
0.00
j-flag
0000000
*-------------------------------------------------------------
*
name
volume
6980000 hp-outpd snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
0. 0.0 0. 1.4 000000
6980101 6.1576 0.5 0.0 -90.
temp
*
cntrl press
9623368. 3469112. 3469112. 1.
6980200 0
junction
*
name
6990000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
0.0 0.0 0000000
6990101 698010000 666000000 0.0
*
cntrl w/v.liq w/v.vap w/v.int
6990201 0 -4.67222-9 -4.67222-9 0. * -1.88798-7
*---------------------------------------------------------
*
Passive DHR Cold leg
lx50% loop
*---------------------------------------------------------
*
name pipe/annulus
6660000 SCS-CL pipe
*
number of volumes
6660001 5
*
area no of vol
6660101 6.1576 5
*
length no of vol
5
6660301 3.7
volume no of vol
*
6660401 0.0
5
*
azi ang no of vol
5
6660501 -90.
*
ver ang no of vol
5
6660601 -90.
*
elev. no of vol
5
6660701 -2.9
*
rough dhydr. no of vol
6660801 4.5e-5 1.6117 5
*
kforw kbackw no of jun
4
6660901 0.0875 0.0875
*
v-flag no of vol
6661001 00000 5
*
j-flag no of jun
6661101 000000 4
*
cntrl pressure temperature * * * no of vol
6661201 0
9644631. 3497396. 3497396. 1. 0. 1
6661202 0
9644697. 3497396. 3497396. 1. 0. 2
6661203 0
9644763. 3497396. 3497396. 1. 0. 3
6661204 0
9644829. 3497396. 3497396. 1. 0. 4
6661205 0
9644895. 3497397. 3497397. 1. 0. 5
cntrl
*
6661300 0
*
w/v.liq w/v.vap w/v.int no of jun
6661301 -9.47945-14 -9.47945-14 0. 1 * -2.729385-13
6661302 -1.594003-13 -1.594003-13 0. 2 * -4.58962-13
6661303 -2.3107-13 -2.3107-13 0. 3 * -6.6533-13
6661304 -2.0602-13 -2.0602-13 0. 4 * -5.93211-13
*
*
*---------------------------------------------------------
* Junction connecting Passive
(simulates
Cold Leg to RPV downcomer with valve
*---------------------------------------------------------
*
name
junction
6670000 hp-ohb valve
*
from
to
area kforw kbackw j-flag
6670101 666010000 670000000 0.0
1.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
6670201 0 0.
0. 0. * 0.
*
valve-type
6670300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
6670301 525 * Close Until end of coastdown
0000000
*---------------------------------------------------------
*
Bypass Junction to simulate leakage of check
check valve
*---------------------------------------------------------
*
name
junction
6950000 leakchv valve
*
from
to
area kforw kbackw j-flag
6950101 666010000 670000000 l.e-9 l.e9 1.e9
*
cntrl w/v.liq w/v.vap w/v.int
6950201 0 0.
0. 0. * 0.
*
valve-type
6950300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
6950301 525 * Close Until end of coastdown
0000000
*
*
*
Passive DHR DECAY HEAT REMOVAL SYSTEM 2 (DHR2)
*
*
*-----------------------------------------------------
*
Junction: Reactor Outlet Plenum to Passive DHR System Duct (DHR2)
*----------------------------------------------
---------
*
name
junction
6060000 opl-hd2 sngljun
*
from
to
area kforw kbackw j-flag
6060101 300010000 611000000 0.0 0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6060201 0 -1.822274-7 -1.822274-7 0. * -6.11274-7
*---------------------------------------------------------
*
Passive DHR Hot Duct (DHR2)
*---------------------------------------------------------
*
name pipe/annulus
6110000 hp-hotd2 pipe
*
number of volumes
6110001 5
*
area no of vol
6110101 2.0774 5
*
length no of vol
6110301 3.8
5
*
volume no of vol
6110401 0.0
5
*
azi ang no of vol
6110501 90.
5
*
ver ang no of vol
6110601 90.
5
elev. no of vol
*
6110701 3.0
5
*
rough dhydr. no of vol
6110801 4.5e-5 1.6264 5
*
kforw kbackw no of jun
6110901 0.0875 0.0875 4
*
v-flag no of vol
6111001 00000 5
*
j-flag no of jun
6111101 000000 4
*
cntrl pressure temperature * * * no of vol
6111201 0
7058062. 3383064. 3383064. 1. 0. 1
6111202 0
7.058+6 3366640. 3366640. 1. 0. 2
6111203 0
7057948. 3341524. 3341524. 1. 0. 3
6111204 0
7057890. 3294012. 3294012. 1. 0. 4
6111205 0
7057830. 3193825. 3193825. 1. 0. 5
*
cntrl
6111300 0
w/v.liq w/v.vap w/v.int no of jun
*
1 * -5.98928-7
6111301 -1.7768-7 -1.7768-7 0.
2 * -5.86226-7
6111302 -1.726138-7 -1.726138-7 0.
3 * -5.72729-7
6111303 -1.6624-7 -1.6624-7 0.
4 * -5.57591-7
6111304 -1.569187-7 -1.569187-7 0.
*
*---------------------------------------------------------
*
Junction: HP Hot Duct to HX POD Inlet (DHR2)
*--------------------------------------------------------
*
name
junction
6160000 hd-hxpi2 sngljun
*
from
to
area kforw kbackw j-flag
6160101 611010000 621000000 0.0 0.75 0.75 0000001
*
cntrl w/v.liq w/v.vap w/v.int
6160201 0 -1.378557-7 -1.378557-7 0. * -5.37921-7
*---------
*
-
-
-
--
---
-
---
-
---
-
---------------
Passive DHR Heat Exchanger POD Inlet (DHR2)
*--------------------------------------------------------
name
volume
*
6210000 hp-hxp2 snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
4.5 0.0 90. 90. 4.5 4.5e-5 1.636 000000 $ 1
6210101 5.4
temp
*
cntrl press
7057717. 2908740. 2908740. 1.
6210200 0
*---------------------------------------------------------
*
Junction: Passive DHR HX POD Inlet to Heat Exchanger Inlet
(DHR2)
*---------------------------------------------------------
junction
*
name
6280000 ihx-hxp2 sngljun
*
from
to
area kforw kbackw j-flag
6280101 621010000 629000000 0.0 0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap .w/v.int
6280201 0 -1.570477-8 -1.570477-8 0. * -3.142066-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Inlet (DHR2)
*---------------------------------------------------------
*
name
volume
6290000 hp-hxin2 snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6290101 2.1276 1.0 0.0 -90.
-90. -0.5 4.5e-5 0.15 000000
*
cntrl press
temp
6290200 0
7057657. 1164302. 1164302. 1.
*---------------------------------------------------------
*
Junction: Passive DHR HX Inlet to Heat Exchanger
(DHR2)
*---------------------------------------------------------
*
name
junction
6300000 ihx-hx sngljun
from
to
area kforw kbackw j-flag
*
6300101 629010000 651000000 0.0 0.23 0.23 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6300201 0 -2.589013-8 -2.589013-8 0. * -3.32553-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger (DHR2)
*---------------------------------------------------------
*
name pipe/annulus
6510000 hp-hx2 pipe
*
number of volumes
6510001 5
*
area no of vol
6510101 2.1856 5
*
length no of vol
6510301 0.060 5
*
volume no of vol
6510401 0.0
5
*
azi ang no of vol
6510501 -90. 5
*
ver ang no of vol
6510601 -90. 5
*
elev. no of vol
$ 1
6510701 -0.06 5
rough dhydr. no of vol
*
6510801 1.e-5 3.055e-3 5
kforw kbackw no of jun
*
0.0
4
6510901 0.0
*
v-flag no of vol
6511001 00000 5
*
j-flag no of jun
6511101 000000 4
*
cntrl pressure temperature * * * no of vol
7057684. 932250. 932250. 1. 0. 1
6511201 0
6511202 0
7057690. 932244. 932244. 1. 0. 2
7057698. 932239. 932239. 1. 0. 3
6511203 0
7057704. 932235. 932235. 1. 0. 4
6511204 0
7057711. 932232. 932232. 1. 0. 5
6511205 0
*
cntrl
6511300 0
*
w/v.liq w/v.vap w/v.int no of jun
6511301 -2.60233-8 -2.60233-8 0. 1 * -3.34266-7
6511302 -2.612243-8 -2.612243-8 0. 2 * -3.35541-7
6511303 -2.618735-8 -2.618735-8 0. 3 * -3.36377-7
6511304 -2.62204-8 -2.62204-8 0. 4 * -3.368025-7
*---------------------------------------------------------
*
Junction: Passive DHR Heat Exchanger to HX Outlet
(DHR2)
*---------------------------------------------------------
*
name
junction
6560000 hx-ohx2 sngljun
to
area kforw kbackw j-flag
from
*
6560101 651010000 668000000 0.0 0.50 0.50 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6560201 0 -4.44103-8 -4.44103-8 0. * -3.37483-7
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Outlet Plenum (DHR2)
*---------------------------------------------------------
*
name
volume
6680000 hp-outp2 snglvol
length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
area
-90.
-0.2 4.5e-5 0.15 000000
6680101 2.1276 1.0 0.0 -90.
temp
press
*
cntrl
7057722. 1573145. 1573145. 1.
6680200 0
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet to Downcomer
(DHR2)
*---------------------------------------------------------
junction
*
name
6690000 hp-ohx2 sngljun
to
area kforw kbackw j-flag
from
*
671000000 0.0 1.0 1.0 0000000
668010000
6690101
*
cntrl w/v.liq w/v.vap w/v.int
6690201 0 -2.11582-8 -2.11582-8 0. * -3.063706-7
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Outlet Pod (DHR2)
*---------------------------------------------------------
name
volume
*
6710000 hp-outp2
length
*
area
snglvol
vol. a.ang. in.ang. elev. rough. hDe
100
v-flag
6710101 10.995 1.0 0.0 -90.
-90.
-1.0 4.5e-5 2.026
*
cntrl press
temp
6710200 0
7057762. 1607285. 1607285. 1.
000000
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet Pod (DHR2)
*---------------------------------------------------------
*
name
junction
6720000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
6720101 671010000 673000000 0.0
0.0 0.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6720201 0 -4.67222-9 -4.67222-9 0. * -1.88798-7
*---------------------------------------------------------
*
Passive DHR
BLOWER (DHR2)
*---------------------------------------------------------
*
name
volume
6730000 hp-outp2 snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe
6730101 6.1576 3.0 0.0 -90. -90.
-3.0 4.5e-5 1.4
*
cntrl press
temp
6730200 0
7057892. 1666776. 1666776. 1.
v-flag
000000
*
*---------------------------------------------------------
*
name
junction
6930000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
6930101 673010000 691000000 0.0
0.0 0.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6930201 0 -4.67222-9 -4.67222-9 0. * -1.88798-7
*
name
volume
6910000 hp-outpc snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
0. 0.0 0. 1.4 000000
6910101 6.1576 0.5 0.0 -90.
*
cntrl press
temp
6910200 0
7057892. 1666776. 1666776. 1.
*
*---------------------------------------------------------
*
name
volume
6940000 hp-outpd snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
6940101 6.1576 0.5 0.0 -90.
0. 0.0 0. 1.4 000000
*
cntrl press
temp
6940200 0
9623368. 3469112. 3469112. 1.
*
*
name
junction
6960000 hp-ohxp sngljun
*
from
to
area kforw kbackw j-flag
6960101 694010000 676000000 0.0
0.0 0.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
6960201 0 -4.67222-9 -4.67222-9 0. * -1.88798-7
*---------------------------------------------------------
*
Valve: Passive DHR
Cold Leg Valve junciton to RPV downcomer (DHR2)
*---------------------------------------------------------
**
name junction
6740000 hp-cl valve
*
from
to
area
kforw
kbackw
101
j-flag
6740101 691010000 694000000 6.1576
*
cntrl w/v.liq w/v.vap w/v.int
6740201 0 0.
0. 0. * 0.
*
valve-type
6740300 mtrvlv
*
trip# w/v.liq w/v.vap w/v.int
0
542
0.0125
0.0
6740301 540
13.46
13.46
00000200
*
*----------------------------------------------------------
Name Valve
**
6880000 leak2 tmdpjun
from
to
*
6880101 694000000 691010000
*
cntrl trp
542
6880200 1
6880201 -0.* 0. 0. 0.
6880201 -0. 0. 0.15 0.
0. 0. 0.15 0.
6880202
area
0.00
j-flag
0000000
*--------------------------------------------------------*---------------------------------------------------------
*
Passive DHR Cold leg
1x50% loop (DHR2)
*---------------------------------------------------------
*
name pipe/annulus
6760000 SCS-CL pipe
*
number of volumes
6760001 5
*
area no of vol
6760101 6.1576 5
*
length no of vol
6760301 3.7
5
*
volume no of vol
6760401 0.0
5
*
azi ang no of vol
6760501 -90.
5
ver ang no of vol
*
6760601 -90.
5
*
elev. no of vol
5
6760701 -2.9
*
rough dhydr. no of vol
6760801 4.5e-5 1.6117 5
*
kforw kbackw no of jun
4
6760901 0.0875 0.0875
*
v-flag no of vol
6761001 00000 5
*
j-flag no of jun
6761101 000000 4
cntrl pressure temperature
*
9623368. 3469112.
6761201 0
9623434. 3469112.
6761202 0
9623500. 3469112.
6761203 0
9623566. 3469113.
6761204 0
9623632. 3469113.
6761205 0
*
cntrl
6761300 0
*
w/v.liq w/v.vap w/v.int no
6761301 -6.67305-15 -6.67305-15
6761302 -3.19196-14 -3.19196-14
* * *
3469112.
3469112.
3469112.
3469113.
3469113.
no
1.
1.
1.
1.
1.
of vol
0. 1
0. 2
0. 3
0. 4
0. 5
of jun
0. 1 * -1.928565-14
0. 2 * -9.22514-14
102
6761303
6761304
-1.173983-13 -1.173983-13 0. 3 * -3.392996-13
8.44969-14 8.44969-14 0. 4 * 2.44209-13
*
*---------------------------------------------------------
*
Valve: Passive DHR
Cold Leg Valve junciton to RPV downcomer (DHR2)
*---------------------------------------------------------
*
name
junction
6770000 hp-ohb2 valve
*
from
to
area kforw kbackw j-flag
6770101 676010000 800000000 0.0
1.0 1.0
*
cntrl w/v.liq w/v.vap w/v.int
6770201 0 0.
0. 0. * 0.
*
valve-type
6770300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
6770301 525 * Close Until end of coastdown
0000000
*---------------------------------------------------------
*
Bypass Junction to simulate leakage of check
check valve
*---------------------------------------------------------
name
junction
6970000 leakchv valve
*
from
to
area kforw kbackw j-flag
6970101 676010000 800000000 1.e-9 l.e9 1.e9
*
cntrl w/v.liq w/v.vap w/v.int
6970201 0 0.
0. 0. * 0.
*
valve-type
6970300 trpvlv
*
trip# w/v.liq w/v.vap w/v.int
6970301 525 * Close Until end of coastdown
*
0000000
*
*
*
Passive DHR DECAY HEAT REMOVAL SYSTEM UHS SYSTEM 1
*
*---------------------------------------------------------
*
H20 DHR Heat Exchanger Inlet
*---------------------------------------------------------
*
name
volume
7000000 h2ohxin snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
7000101 0.0873 1.0 0.0 90. 90. 0.5 4.5e-5 0.333 000000
*
cntrl press
temp
7000200 0
1085604. 104058.9 2584130. 0.
*--------------------------------------------------------*
Junction: H20 Passive DHR HX Inlet to Heat Exchanger
*---------------------------------------------------------
name
junction
7050000 h2oihxj sngljun
*
from
to
area kforw kbackw j-flag
7050101 700010000 710000000 0.0 0.23 0.23
*
cntrl w/v.liq w/v.vap w/v.int
7050201 0 8.28489-4 8.3558-4 0. * .0721563
*
*
*-------------------------------------------
103
0000000
*
Passive H20 DHR Heat Exchanger
*---------------------------------------------------------
name pipe/annulus
*
7100000 h2ohphx pipe
number of volumes
*
7100001 5
*
area no of vol
7100101 1.09281 5
*
length no of vol
7100301 0.060 5
*
volume no of vol
5
7100401 0.0
azi ang no of vol
*
7100501 90.
5
*
ver ang no of vol
5
7100601 90.
*
elev. no of vol
7100701 0.060 5
*
rough dhydr. no of vol
7100801 1.e-5 3.055e-3 5
kforw kbackw no of jun
*
4
0.0
7100901 0.0
*
v-flag no of vol
7101001 00000 5
j-flag no of jun
*
7101101 000000 4
cntrl pressure temperature * * * no of vol
*
1082864. 104068.4 2584060. 0. 0. 1
7101201 0
1082277. 104073. 2584045. 0. 0. 2
7101202 0
1081690. 104078.7 2584030. 0. 0. 3
7101203 0
1081103. 104085.5 2584014. 0. 0. 4
7101204 0
1080516. 104093. 2.584+6 0. 0. 5
7101205 0
*
cntrl
7101300 0
w/v.liq w/v.vap w/v.int no of jun
*
1 * .0721563
7101301 6.61846-5 6.62321-5 0.
2 * .0721563
7101302 6.61846-5 6.62321-5 0.
3 * .0721563
7101303 6.61846-5 6.62321-5 0.
4 * .0721563
7101304 6.61847-5 6.62322-5 0.
*
*---------------------------------------------------------
*
Junction: H20 Passive DHR Heat Exchanger to HX Outlet
*---------------------------------------------------------
junction
*
name
7150000 h2hxohx sngljun
area kforw kbackw j-flag
to
*
from
7150101 710010000 720000000 0.0 1.00 1.00
cntrl w/v.liq w/v.vap w/v.int
*
7150201 0 8.28492-4 8.35584-4 0. * .0721563
0000000
*
*--------------------------------------------------------
*
Passive H20 DHR Heat Exchanger Outlet Plenum
*---------------------------------------------------------
volume
*
name
7200000 h2ooutpl snglvol
length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
area
7200101 0.0873 1.0 0.0 90. 90. 0.2 4.5e-5 0.333 000000
104
*
cntrl press
temp
7200200 0
1079244. 104098. 2583967. 0.
*
*---------------------------------------------------------
*
Junction: H20 DHR Heat Exchanger Outlet Plenum to UHS Duct
*---------------------------------------------------------
junction
*
name
7250000 h2oplhd sngljun
*
from
to
area kforw kbackw j-flag
7250101 720010000 730000000 0.0 0.23 0.23
cntrl w/v.liq w/v.vap w/v.int
*
7250201 0 8.28492-4 8.35584-4 0. * .0721563
0000000
*
*---------------------------------------------------------
*
Passive DHR Hot Duct
*---------------------------------------------------------
*
name pipe/annulus
7300000 h2ohotd pipe
*
number of volumes
7300001 5
*
area no of vol
7300101 0.0873 5
*
length no of vol
7300301 1.6
5
*
volume no of vol
7300401 0.0
5
*
azi ang no of vol
7300501 90.
5
ver ang no of vol
*
7300601 90.
5
elev. no of vol
*
7300701 1.6
5
*
rough dhydr. no of vol
7300801 4.5e-5 0.333 5
kforw kbackw no of jun
*
7300901 0.0875 0.0875 4
*
v-flag no of vol
7301001 00000 5
j-flag no of jun
*
7301101 000000 4
cntrl pressure temperature * * * no of vol
*
7301201 0
1070439. 104106.3 2583740. 0. 0. 1
7301202 0
1054786. 104114.7 2583334. 0. 0. 2
7301203 0
1039133. 104123.5 2582923. 0. 0. 3
7301204 0
1023479. 104133.1 2582507. 0. 0. 4
7301205 0
1007826. 104160.4 2582086. 3.71865-6 0. 5
*
cntrl
7301300 0
*
w/v.liq w/v.vap w/v.int no of jun
7301301 8.28495-4 8.35587-4 0.
1 * .0721562
7301302 8.28501-4 8.35593-4 0.
2 * .0721562
7301303 8.28507-4 8.35599-4 0.
3 * .0721561
7301304 8.28513-4 .00157848 0.
4 * .0721561
*
**---------------------------------------------------------
**
Junction: Hotleg Duct to surge tank
**---------------------------------------------------------
105
**
name type
7800000 h2o-surj sngljun
area kforw kbackw j-flag
*
from
to
7800101 730010000 790000000 0
0.5 0.5 0000000
*
cntrl w/v.liq w/v.vap w/v.int
7800201 0 -.00146826 -9.44189-7 0. * -4.00458-7
*
*---------------------------------------------------------
**
H20 LOOP surge tank
*---------------------------------------------------------
*
name
volume
7900000 h20surge tmdpvol
*
area length vol. a.ang. in.ang. elev. rough. hDe pvbfe
7900101 500.0 10.0 0.0 0.0 0.0 0. 0.00046 7.4 00010
*
cntrl
7900200 003
*
press temp
7900201 0.0 1.00000e6 473.0
*--------------------------------------------------------*
Junction: HP Hot Duct to HX Inlet
*---------------------------------------------------------
*
name
junction
7350000 h2ohxpin sngljun
*
from
to
area kforw kbackw j-flag
7350101 730010000 740000000 0.0 0.75 0.75
*
cntrl w/v.liq w/v.vap w/v.int
7350201 0 8.28526-4
.02027343 0. * .0721564
0000001
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Inlet
*---------------------------------------------------------
*
name
volume
7400000 h2ohxin snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
-90.
-0.5 4.5e-5 0.333 000000
7400101 0.0873 1.0 0.0 -90.
*
cntrl press
temp
7400200 0
1002446. 104171.3 2581940. 1.404818-6
*---------------------------------------------------------
*
Junction: Passive DHR HX Inlet to Heat Exchanger
*---------------------------------------------------------
*
name
junction
7450000 h2ohx-h sngljun
*
from
to
area kforw kbackw j-flag
7450101 740010000 750000000 0.0 0.23 0.23
*
cntrl w/v.liq w/v.vap w/v.int
7450201 0 8.28526-4 -.00344602 0. * .0721564
*
*---------------------------------------------------------
*
Passive H20/UHS
Heat Exchanger
*---------------------------------------------------------
*
name pipe/annulus
7500000 h2hp-hx pipe
*
number of volumes
7500001 20
*
area no of vol
7500101 9.64974e-2 20
*
length no of vol
106
0000000
7500301 1.605 20
*
volume no of vol
7500401 0.0
20
*
azi ang no of vol
20
7500501 -90.
*
ver ang no of vol
7500601 0.0
20
*
elev. no of vol
7500701 0.0
20
*
rough dhydr. no of vol
7500801 1.e-5 3.5052e-2 20
kforw kbackw no of jun
*
7500901 0.0
0.0
19
*
v-flag no of vol
7501001 00000 20
*
j-flag no of jun
7501101 000000 19
*
cntrl pressure temperature * * * no of
7501201 0
1004892. 104080.5 2582007. 0. 0.
1004892. 104063. 2582007. 0. 0.
7501202 0
1004892. 104059.6 2582007. 0. 0.
7501203 0
1004891. 104059. 2582007. 0. 0.
7501204 0
7501205 0
1004891. 104058.8 2582007. 0. 0.
1004891. 104058.8 2582007. 0. 0.
7501206 0
7501207 0
1004891. 104058.8 2582007. 0. 0.
7501208 0
1004891. 104058.8 2582007. 0. 0.
1004891. 104058.8 2582007. 0. 0.
7501209 0
1004891. 104058.8 2582007. 0. 0.
7501210 0
1004891. 104058.8 2582007. 0. 0.
7501211 0
7501212 0
1004891. 104058.8 2582007. 0. 0.
7501213 0
1004891. 104058.8 2582007. 0. 0.
1004891. 104058.8 2582007. 0. 0.
7501214 0
7501215 0
1004891. 104058.8 2582007. 0. 0.
1004891. 104058.8 2582007. 0. 0.
7501216 0
7501217 0
1004891. 104058.8 2582007. 0. 0.
7501218 0
1004891. 104058.8 2582007. 0. 0.
7501219 0
1004891. 104058.8 2582007. 0. 0.
7501220 0
1004891. 104058.8 2582007. 0. 0.
*
cntrl
7501300 0
*
w/v.liq w/v.vap w/v.int no of jun
7501301 7. 49551-4 7.49551-4 0.
1 * .0721563
7501302 7. 4955-4 7.4955-4 0.
2 * .0721563
3 * .0721563
7501303 7. 4955-4 7.4955-4 0.
4 * .0721563
7501304 7. 4955-4 7.4955-4 0.
5 * .0721563
7501305 7. 4955-4 7.4955-4 0.
7501306 7. 4955-4 7.4955-4 0.
6 * .0721563
7 * .0721563
7501307 7. 4955-4 7.4955-4 0.
7501308 7. 4955-4 7.4955-4 0.
8 * .0721563
9 * .0721563
7501309 7. 4955-4 7.4955-4 0.
7501310 7. 4955-4 7.4955-4 0.
10 * .0721563
11 * .0721563
7501311 7. 4955-4 7.4955-4 0.
7501312 7. 4955-4 7.4955-4 0.
12 * .0721563
7501313 7. 4955-4 7.4955-4 0.
13 * .0721563
7501314 7. 4955-4 7.4955-4 0.
14 * .0721563
7501315 7. 4955-4 7.4955-4 0.
15 * .0721563
7501316 7. 4955-4 7.4955-4 0.
16 * .0721563
107
vol
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
7501317
7501318
7501319
7.4955-4
7.4955-4
7.4955-4
7.4955-4
7.4955-4
7.4955-4
0.
0.
0.
17 * .0721563
18 * .0721563
19 * .0721563
*
*---------------------------------------------------------
*
Junction: H20/UHS Passive DHR Heat Exchanger to HX Outlet
*---------------------------------------------------------
junction
*
name
7550000 h2hx-ohx sngljun
area kforw kbackw j-flag
to
*
from
7550101 750010000 760000000 0.0 1.00 1.00
*
cntrl w/v.liq w/v.vap w/v.int
7550201 0 8.28518-4 8.28518-4 0. * .0721563
0000000
*
*---------------------------------------------------------
*
Passive UHS DHR Heat Exchanger Outlet Plenum
*---------------------------------------------------------
name
volume
7600000 h2-outpl snglvol
area
length vol. a.ang. in.ang. elev. rough.
*
-0.5 4.5e-5
-90.
7600101 0.0873 1.0 0.0 -90.
*
cntrl press
temp
1007337. 104058.8 2582073. 0.
7600200 0
*
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet to Downcomer
*---------------------------------------------------------
junction
name
sngljun
hhp-ohx
7650000
area kforw kbackw j-flag
to
*
from
7650101 760010000 770000000 0.0 1.0 1.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
7650201 0 8.28517-4 8.3561-4 0. * .0721563
*
*---------------------------------------------------------
*
Passive DHR Downcomer
*---------------------------------------------------------
name pipe/annulus
7700000 h2ohotd pipe
*
number of volumes
7700001 5
area no of vol
*
7700101 0.0873 5
length no of vol
*
5
7700301 1.6
volume no of vol
*
5
7700401 0.0
*
azi ang no of vol
5
7700501 -90.
*
ver ang no of vol
5
7700601 -90.
elev. no of vol
*
7700701 -1.6 5
*
rough dhydr. no of vol
7700801 4.5e-5 0.333 5
*
kforw kbackw no of jun
7700901 0.0875 0.0875 4
*
v-flag no of vol
*
108
hDe v-flag
0.333 000000
7701001 00000 5
*
j-flag no of jun
7701101 000000 4
*
cntrl pressure temperature
1017609. 104058.8
7701201 0
7701202 0
1033262. 104058.8
1048916. 104058.8
7701203 0
7701204 0
1064569. 104058.8
7701205 0
1080223. 104058.9
*
cntrl
7701300 0
*
w/v.liq w/v.vap w/v.int no
7701301 8.28514-4 8.35606-4 0.
7701302 8.28508-4 8.356-4 0.
7701303 8.28502-4 8.35594-4 0.
7701304 8.28496-4 8.35589-4 0.
* * *
2582350.
2582768.
2583181.
2583589.
2583992.
no
0.
0.
0.
0.
0.
of vol
0. 1
0. 2
0. 3
0. 4
0. 5
of jun
1 * .0721563
2 * .0721563
3 * .0721563
4 * .0721563
*---------------------------------------------------------
*
SNGLJ: Passive DHR Cold Duct to Rx Inlet Plenum
*---------------------------------------------------------
*
name
junction
7750000 cd-iplm sngljun
*
from
to
area kforw kbackw j-flag
7750101 770010000 700000000 0.0 1.0 1.0 0000001
*
cntrl w/v.liq w/v.vap w/v.int
7750201 0 8.2849-4 8.2849-4 0. * .0721563
*
*
*
Passive DHR DECAY HEAT REMOVAL SYSTEM UHS SYSTEM 2-Water loop
*
*---------------------------------------------------------
*
H20 DHR Heat Exchanger Inlet (DHR2-Water)
*---------------------------------------------------------
*
name
volume
7010000 h2ohxin snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
7010101 0.0873 1.0 0.0 90. 90. 0.5 4.5e-5 0.333 000000
*
cntrl press
temp
7010200 0
1085604. 104059. 2584130. 0.
*---------------------------------------------------------
*
Junction: H20 Passive DHR HX Inlet to Heat Exchanger (DHR2-Water)
*---------------------------------------------------------
*
name
junction
7060000 h2oihxj
sngljun
*
from
to
area kforw kbackw j-flag
7060101 701010000 711000000 0.0 0.23 0.23
*
cntrl w/v.liq w/v.vap w/v.int
7060201 0 7.98759-4 8.05363-4 0. * .0695671
0000000
*
*---------------------------------------------------------
* Passive H20 DHR Heat Exchanger (DHR2-Water)
*--------------------------------------------------------*
name
pipe/annulus
109
7110000 h2ohphx pipe
*
number of volumes
7110001 5
*
area no of vol
7110101 1.09281 5
*
length no of vol
7110301 0.060 5
*
volume no of vol
7110401 0.0
5
*
azi ang no of vol
7110501 90.
5
*
ver ang no of vol
7110601 90.
5
elev. no of vol
*
7110701 0.060 5
*
rough dhydr. no of vol
7110801 l.e-5 3.055e-3 5
*
kforw kbackw no of jun
7110901 0.0
0.0
4
*
v-flag no of vol
7111001 00000 5
*
j-flag no of jun
7111101 000000 4
*
cntrl pressure temperature * * * no of vol
7111201 0
1082864. 104067. 2584060. 0. 0. 1
7111202 0
1082277. 104071.2 2584045. 0. 0. 2
7111203 0
1081690. 104076.7 2584030. 0. 0. 3
7111204 0
1081103. 104083.6 2584014. 0. 0. 4
7111205 0
1080516. 104092. 2.584+6 0. 0. 5
*
cntrl
7111300 0
of jun
*
w/v.liq w/v.vap w/v.int
1 * 069567
7111301 6.38096-5 6.38538-5
069567
2*
7111302 6.38096-5 6.38538-5
3*
069567
7111303 6.38097-5 6.38538-5
4*
069567
7111304 6.38097-5 6.38538-5
*--------------------------------------------
*
Junction: H20 Passive DHR Heat Exchanger to HX Outlet
(DHR2-Water)
*---------------------------------------------------------
*
name
junction
7160000 h2hxohx sngljun
*
from
to
area kforw kbackw j-flag
7160101 711010000 721000000 0.0 1.00 1.00
*
cntrl w/v.liq w/v.vap w/v.int
7160201 0 7.98762-4 8.05366-4 0. * .069567
0000000
*
*---------------------------------------------------------
*
Passive H20 DHR Heat Exchanger Outlet Plenum (DHR2-Water)
*---------------------------------------------------------
*
name
volume
7210000 h2ooutpl snglvol
*
area
length vol. a.ang. in.ang. elev. rough. hDe v-flag
90. 0.2 4.5e-5 0.333 000000 $
7210101 0.0873 1.0 0.0 90.
*
cntrl press
temp
7210200 0
1079244. 104097.8 2583967. 0.
110
*------------------------------------------------------
* Junction: H20 DHR Heat Exchanger Outlet Plenum to UHS Duct
Water)
*---------------------------------------------------------
name
junction
*
7260000 h2oplhd sngljun
to
area kforw kbackw j-flag
*
from
7260101 721010000 731000000 0.0 0.23 0.23
cntrl w/v.liq w/v.vap w/v.int
*
7260201 0 7.98762-4 8.05366-4 0. * .069567
0000000
*
*
*---------------------------------------------------------
*
Passive DHR Hot Duct (DHR2-Water)
*---------------------------------------------------------
*
name pipe/annulus
7310000 h2ohotd pipe
number of volumes
*
7310001 5
*
area no of vol
7310101 0.0873 5 $ lumping 2 loops
*
length no of vol
7310301 1.6
5
*
volume no of vol
5
7310401 0.0
*
azi ang no of vol
7310501 90.
5
ver ang no of vol
*
7310601 90.
5
elev. no of vol
*
7310701 1.6
5
*
rough dhydr. no of vol
7310801 4.5e-5 0.333 5
*
kforw kbackw no of jun
7310901 0.0875 0.0875 4
*
v-flag no of vol
7311001 00000 5
*
j-flag no of jun
7311101 000000 4
*
cntrl pressure temperature * * * no of vol
7311201 0
1070439. 104108.4 2583740. 0. 0. 1
7311202 0
1054786. 104120.5 2583334. 0. 0. 2
7311203 0
1039133. 104134. 2582923. 0. 0. 3
7311204 0
1023480. 104149.5 2582507. 0. 0. 4
7311205 0
1007826. 104168.6 2582086. 0. 0. 5
*
cntrl
7311300 0
*
w/v.liq w/v.vap w/v.int no of jun
7311301 7.98765-4 8.0537-4 0.
1 * .069567
7311302 7.98771-4 8.05375-4 0.
2 * .0695669
7311303 7.98776-4 8.05381-4 0.
3 * .0695668
7311304 7.98782-4 8.05387-4 0.
4 * .0695668
*
**---------------------------------------------------------
** Junction: Hotleg Duct to Pressure Controller (DHR2-Water)
**--------------------------------------------------------**
name
type
111
(DHR2-
7810000 htdc-orf sngljun
*
from
to
area kforw kbackw j-flag
7810101 731010000 791000000 0
0.5 0.5 0000000
*
cntrl w/v.liq w/v.vap w/v.int
7810201 0 -5.48151-9 -5.4809-9 0. * -4.67351-7
*
*---------------------------------------------------------
**
UHS LOOP Pressure Controller
(DHR2-Water)
*---------------------------------------------------------
*
name
volume
7910000 h20surge tmdpvol
*
area length vol. a.ang. in.ang. elev. rough. hDe pvbfe
7910101 500.0 10.0 0.0 0.0 0.0 0. 0.00046 7.4 00010
*
cntrl
7910200 003
press temp
*
7910201 0.0 1.00000e6 345.67
*---------------------------------------------------------
*
Junction: HP Hot Duct to HX Inlet
(DHR2-Water)
*---------------------------------------------------------
*
name
junction
7360000 h2ohxpin sngljun
to
area kforw kbackw j-flag
*
from
7360101 731010000 741000000 0.0 0.75 0.75
*
cntrl w/v.liq w/v.vap w/v.int
7360201 0 7.98793-4 7.98793-4 0. * .0695672
0000001
*
*---------------------------------------------------------
*
Passive DHR Heat Exchanger Inlet (DHR2-Water)
*---------------------------------------------------------
*
name
volume
7410000 h2ohxin snglvol
length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
area
-90.
-0.5 4.5e-5 0.333 000000
7410101 0.0873 1.0 0.0 -90.
*
cntrl press
temp
1002446. 104180.8 2581940. 0.
7410200 0
*---------------------------------------------------------
*
Junction: Passive DHR HX Inlet to Heat Exchanger
(DHR2-Water)
*---------------------------------------------------------
name
junction
*
7460000 h2ohx-h sngljun
area kforw kbackw j-flag
*
from
to
7460101 741010000 751000000 0.0 0.23 0.23
*
cntrl w/v.liq w/v.vap w/v.int
7460201 0 7.98795-4 7.98795-4 0. * .0695671
*
*---------------------------------------------------------
*
Passive UHS DHR Heat Exchanger
(DHR2-Water)
*---------------------------------------------------------
name pipe/annulus
*
7510000 h2hp-hx pipe
*
number of volumes
7510001 20
*
area no of vol
7510101 9.46497e-2 20
*
length no of vol
7510301 1.605 20
112
0000000
$
*
volume no of vol
7510401 0.0
20
*
azi ang no of vol
7510501 -90. 20
*
ver ang no of vol
7510601 0.0
20
*
elev. no of vol
7510701 0.0
20
*
rough dhydr. no of vol
7510801 1.e-5 3.5052e-2 20
*
kforw kbackw no of jun
7510901 0.0
0.0
19
v-flag no of vol
*
7511001 00000 20
*
j-flag no of jun
7511101 000000 19
*
cntrl pressure temperature * * * no of vol
7511201 0
1004892. 104081.7 2582007. 0. 0. 1
7511202 0
1004892. 104063.2 2582007. 0. 0. 2
7511203 0
1004892. 104059.7 2582007. 0. 0. 3
7511204 0
1004892. 104059. 2582007. 0. 0. 4
7511205 0
1004891. 104058.8 2582007. 0. 0. 5
7511206 0
1004891. 104058.8 2582007. 0. 0. 6
7511207 0
1004891. 104058.8 2582007. 0. 0. 7
7511208 0
1004891. 104058.8 2582007. 0. 0. 8
7511209 0
1004891. 104058.8 2582007. 0. 0. 9
7511210 0
1004891. 104058.8 2582007. 0. 0. 10
7511211 0
1004891. 104058.8 2582007. 0. 0. 11
7511212 0
1004891. 104058.8 2582007. 0. 0. 12
7511213 0
1004891. 104058.8 2582007. 0. 0. 13
7511214 0
1004891. 104058.8 2582007. 0. 0. 14
7511215 0
1004891. 104058.8 2582007. 0. 0. 15
7511216 0
1004891. 104058.8 2582007. 0. 0. 16
7511217 0
1004891. 104058.8 2582007. 0. 0. 17
7511218 0
1004891. 104058.8 2582007. 0. 0. 18
7511219 0
1004891. 104058.8 2582007. 0. 0. 19
7511220 0
1004891. 104058.8 2582007. 0. 0. 20
cntrl
*
7511300 0
*
w/v.liq w/v.vap w/v.int no of jun
7511301 7.36762-4 7.36762-4 0. 1 * .0695671
7511302 7.36761-4 7.36761-4 0. 2 * .0695671
7511303 7.3676-4 7.3676-4 0.
3 * .0695671
7511304 7.3676-4 7.3676-4 0.
4 * .0695671
7511305 7.3676-4 7.3676-4 0.
5 * .0695671
7511306 7.3676-4 7.3676-4 0.
6 * .0695671
7511307 7.3676-4 7.3676-4 0.
7 * .0695671
7511308 7.3676-4 7.3676-4 0.
8 * .0695671
7511309 7.3676-4 7.3676-4 0.
9 * .0695671
7511310 7.3676-4 7.3676-4 0.
10 * .0695671
7511311 7.3676-4 7.3676-4 0.
11 * .0695671
7511312 7.3676-4 7.3676-4 0.
12 * .0695671
7511313 7.3676-4 7.3676-4 0.
13 * .0695671
7511314 7.3676-4 7.3676-4 0.
14 * .0695671
7511315 7.3676-4 7.3676-4 0.
15 * .0695671
7511316 7.3676-4 7.3676-4 0.
16 * .0695671
7511317 7.3676-4 7.3676-4 0.
17 * .0695671
113
7511318
7511319
7.3676-4
7.3676-4
7.3676-4 0.
7.3676-4 0.
18 * .0695671
19 * .0695671
*
*---------------------------------------------------------
*
Junction: UHS Passive DHR Heat Exchanger to HX Outlet
*---------------------------------------------------------
name
junction
7560000 h2hx-ohx sngljun
*
from
to
area kforw kbackw j-flag
7560101 751010000 761000000 0.0 1.00 1.00
cntrl w/v.liq w/v.vap w/v.int
*
7560201 0 7.98788-4 7.98788-4 0. * .0695671
*
0000000
*
*---------------------------------------------------------
*
Passive UHS DHR Heat Exchanger Outlet Plenum
*---------------------------------------------------------
name
volume
7610000 h2-outpl snglvol
length vol. a.ang. in.ang. elev. rough. hDe v-flag
*
area
-0.5 4.5e-5 0.333 000000
7610101 0.0873 1.0 0.0 -90.
-90.
*
cntrl press
temp
1007337. 104058.8 2582073. 0.
7610200 0
*
*
*---------------------------------------------------------
*
Junction: Passive DHR HX Outlet to Downcomer
*---------------------------------------------------------
junction
name
7660000 hhp-ohx sngljun
to
area kforw kbackw j-flag
*
from
7660101 761010000 771000000 0.0 1.0 1.0 0000000
*
cntrl w/v.liq w/v.vap w/v.int
7660201 0 7.98787-4 8.05391-4 0. * .0695671
*
*---------------------------------------------------------
*
Passive DHR Downcomer
*---------------------------------------------------------
name pipe/annulus
7710000 h2ohotd pipe
*
number of volumes
7710001 5
*
area no of vol
7710101 0.0873 5 $ lumping 2 loops
*
length no of vol
5
7710301 1.6
volume no of vol
*
5
7710401 0.0
*
azi ang no of vol
7710501 -90.
5
*
ver ang no of vol
5
7710601 -90.
elev. no of vol
*
7710701 -1.6 5
rough dhydr. no of vol
*
7710801 4.5e-5 0.333 5
*
kforw kbackw no of jun
7710901 0.0875 0.0875 4
*
*
v-flag
7711001
no of vol
00000
5
114
$
*
j-flag no of jun
7711101 000000 4
*
cntrl pressure temperature * * * no of
7711201 0
1017609. 104058.8 2582350. 0. 0.
7711202 0
1033263. 104058.8 2582768. 0. 0.
7711203 0
1048916. 104058.8 2583181. 0. 0.
7711204 0
1064569. 104058.8 2583589. 0. 0.
7711205 0
1080223. 104058.9 2583992. 0. 0.
*
cntrl
7711300 0
*
w/v.liq w/v.vap w/v.int no of jun
7711301 7.98783-4 8.05388-4 0.
1 * .0695671
7711302 7.98778-4 8.05382-4 0.
2 * .0695671
7711303 7.98772-4 8.05376-4 0.
3 * .0695671
7711304 7.98766-4 8.05371-4 0.
4 * .0695671
vol
1
2
3
4
5
*
*---------------------------------------------------------
*
SNGLJ: Passive DHR Cold Duct to Rx Inlet Plenum
*---------------------------------------------------------
*
name
junction
7760000 cd-iplm sngljun
*
from
to
area kforw kbackw j-flag
7760101 771010000 701000000 0.0 1.0 1.0 0000001
*
cntrl w/v.liq w/v.vap w/v.int
7760201 0 7.98761-4 7.98761-4 0. * .0695671
*
*
*
HEAT STRUCTURE COMPONENTS
*
*
*
RPV Downcomer (Cylinder)
# Wall thickness: 0.014m
*
#1
*
*
#-HS #-MP geotype SS-ini L-coord. reflood
16701000 8 10 2
0 4.0
*
mesh-loc format-flag
16701100 0
1
*
#-Intvl R-coord. (radial info.)
16701101 9
4.19
*
comp-# interval-# (radial info.)
16701201 6
9
*
source interval-# (radial info.)
16701301 0.0
9
*
initial temperature flag (if flag=0 or -1)
115
bvol-ind axial#
16701400 -1
*
temp-i temp-2 temp-3 temp-4 temp-5 temp-6 temp-7 temp-8 temp-9
temp-i
16701401 740.49 740.50 740.50 740.50 740.50 740.50 740.51 740.51 740.51
740.51
16701402 740.50 740.51 740.51 740.51 740.52 740.52 740.52 740.53 740.53
740.53
16701403 740.51 740.52 740.52 740.53 740.53 740.54 740.54 740.54 740.55
740.55
16701404 740.52 740.53 740.54 740.54 740.55 740.56 740.56 740.56 740.57
740.57
16701405 740.53 740.54 740.55 740.56 740.57 740.57 740.58 740.58 740.59
740.59
16701406 740.54 740.55 740.56 740.57 740.58 740.59 740.60 740.60 740.60
740.61
16701407 740.55 740.56 740.58 740.59 740.60 740.61 740.62 740.62 740.62
740.62
16701408 740.56 740.57 740.59 740.60 740.61 740.62 740.63 740.64 740.64
740.64
* L-B B.Vol.#
increment BC option surf.code height NH
1
1.05625 8
160
16701501 670010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
1.05625 8 * Insulate
0
1
0
16701601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
8
0.
0.
0.
16701701 0
*
9-words format option
16701800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
* Add L-B Dh HL-f
0. 0. 1. 1
16701801 8.000 0.528125 20. 0. 0.
0. 0. 1. 2
16701802 8.000 1.584375 20. 0. 0.
0. 0. 1. 3
16701803 8.000 2.640625 20. 0. 0.
0. 0. 1. 4
16701804 8.000 3.696875 20. 0. 0.
0. 0. 1. 5
16701805 8.000 4.753125 20. 0. 0.
0. 0. 1. 6
16701806 8.000 5.809375 20. 0. 0.
0. 0. 0. 0. 1. 7
16701807 8.000 6.865625 20.
0. 0. 0. 0. 1. 8
16701808 8.000 7.921875 20.
HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
* Add R-B Dh HL-f
0. 0. 1. 1
16701901 8.380 0.528125 20. 0. 0.
0. 0. 1. 2
16701902 8.380 1.584375 20. 0. 0.
20.
0.
0.
0. 0. 1. 3
16701903 8.380 2.640625
0.
0. 0. 1. 4
20.
0.
16701904 8.380 3.696875
0. 0. 1. 5
16701905 8.380 4.753125 20. 0. 0.
0. 0. 1. 6
16701906 8.380 5.809375 20. 0. 0.
0. 0. 1. 7
16701907 8.380 6.865625 20. 0. 0.
0. 0. 1. 8
16701908 8.380 7.921875 20. 0. 0.
*---------------------------------
*
*
RPV Downcomer (Cylinder)
# Wall thickness: 0.014m
*
#-HS #-MP geotype SS-ini L-coord. reflood
0 4.0
18001000 8 10 2
*
mesh-loc format-flag
1
18001100 0
#-Intvl R-coord. (radial info.)
*
4.19
18001101 9
116
bvol-ind axial#
*
comp-# interval-# (radial info.)
18001201 6
9
*
source interval-# (radial info.)
9
18001301 0.0
initial temperature flag (if flag=0 or -1)
*
18001400 -1
*
temp-i temp-2 temp-3 temp-4 temp-5 temp-6 temp-7 temp-8 temp-9
temp-i
18001401 740.49 740.50 740.50 740.50 740.50 740.50 740.51 740.51 740.51
740.51
18001402 740.50 740.51 740.51 740.51 740.52 740.52 740.52 740.53 740.53
740.53
18001403 740.51 740.52 740.52 740.53 740.53 740.54 740.54 740.54 740.55
740.55
18001404 740.52 740.53 740.54 740.54 740.55 740.56 740.56 740.56 740.57
740.57
18001405 740.53 740.54 740.55 740.56 740.57 740.57 740.58 740.58 740.59
740.59
18001406 740.54 740.55 740.56 740.57 740.58 740.59 740.60 740.60 740.60
740.61
18001407 740.55 740.56 740.58 740.59 740.60 740.61 740.62 740.62 740.62
740.62
18001408 740.56 740.57 740.59 740.60 740.61 740.62 740.63 740.64 740.64
740.64
* L-B B.Vol.#
increment BC option surf.code height NH
160
1
1.05625 8
18001501 800010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
18001601 0
0
0
1
1.05625 8 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
0.
8
0.
18001701 0
*
9-words format option
18001800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
* Add L-B Dh HL-f
18001801 8.000 0.528125 20. 0. 0. 0. 0.
1. 1
18001802 8.000 1.584375 20. 0. 0. 0. 0.
1. 2
1. 3
18001803 8.000 2.640625 20. 0. 0. 0. 0.
18001804 8.000 3.696875 20. 0. 0. 0. 0.
1. 4
18001805 8.000 4.753125 20. 0. 0. 0. 0.
1. 5
18001806 8.000 5.809375 20. 0. 0. 0. 0.
1. 6
18001807 8.000 6.865625 20. 0. 0. 0. 0.
1. 7
18001808 8.000 7.921875 20. 0. 0. 0. 0.
1. 8
* Add R-B Dh HL-f
HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
18001901 8.380 0.528125 20. 0. 0. 0.
0. 1. 1
18001902 8.380 1.584375 20. 0. 0. 0. 0. 1. 2
18001903 8.380 2.640625 20. 0. 0. 0. 0. 1. 3
18001904 8.380 3.696875 20. 0. 0.
0. 0. 1. 4
18001905 8.380 4.753125 20. 0. 0. 0. 0. 1. 5
18001906 8.380 5.809375 20. 0. 0. 0. 0. 1. 6
18001907 8.380 6.865625 20. 0. 0. 0. 0. 1. 7
18001908 8.380 7.921875 20. 0. 0. 0. 0. 1. 8
*
*--------------------------------*
Tr~I~i-
DI~rmrn
tr~7iivr~-v-~
*
)
(
Plenum
Inlet
*
*
*
# Wall thickness: 0.004m
#-HS
#-MP
geotype SS-ini L-coord. reflood
117
bvol-ind axial#
11001000 5 5 2
0 0.0
* mesh-loc
format-flag
11001100 0
1
* #-Intvl
R-coord. (radial info.)
11001101 4
0.075
* comp-#
interval-# (radial info.)
11001201 6
* source value
interval-# (radial info.)
11001301 0.0
4
* initial temperature flag (if flag=0 or -1)
11001400 -1
temp-3 temp-4 temp-5
*
temp-1 temp-2
11001401 740.50 740.50 740.50 740.50 740.50
11001402 740.50 740.50 740.50 740.50 740.50
11001403 740.50 740.50 740.50 740.50 740.50
11001404 740.50 740.50 740.50 740.50 740.50
11001405 740.50 740.50 740.50 740.50 740.50
* L-B B.Vol.#
increment BC option surf.code height NH
11001501 0
0
0
1
0.2
5 * Insulate
* R-B B.Vol.#
increment BC option surf.code height NH
11001601 100010000 10000
160
1
0.2
5
* Source source-type multiplier DHeat-Left DHeat-Right NH
11001701 0
0.
0.
0.
5
* Add R-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
11001901 0.150 0.1 20. 0. 0. 0. 0. 1. 1
11001902 0.150 0.3 20. 0. 0. 0. 0. 1. 2
11001903 0.150 0.5 20. 0. 0. 0. 0. 1. 3
11001904 0.150 0.7 20. 0. 0. 0. 0. 1. 4
11001905 0.150 0.9 20. 0. 0. 0. 0. 1. 5
*
Lower Reflector-Entrance of Core Average Channel (Plate)
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
*
12101000 1 3 1
0
0.0
*
mesh-loc format-flag
12101100 0
1
*
#-Intvl R-coord. (radial info.)
12101101 2
0.002655
comp-# interval-# (radial info.)
*
12101201 13
2
*
source value interval-# (radial info.)
12101301 0.0
2
*
initial temperature flag (if flag=0 or -1)
12101400 -1
*
temp-1 temp-2 temp-3
12101401 740.62 740.62 740.62
increment BC option surf.code area NH
* L-B B.Vol.#
439.62 1 * Insulat
0
0
1
12101501 0
increment BC option surf.code area NH
* R-B B.Vol.#
1
439.62 1
160
12101601 210010000 10000
* Source source-type multiplier DHeat-Left DHeat-Right NH
1
0.
0.
0.
12101701 0
*
9-words format option
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
* Add R-B Dh
12101901 0.0127 0.5 20. 0. 0. 0. 0. 1. 1
*
*====
=-=-
==
==
-=
===
===-
==
====
==-
118
===
===
====
===-
==
===
*
Lower Reflector-Entrance of Core Hot Channel
(Plate)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
12111000 1 3 1
0 0.0
mesh-loc format-flag
*
12111100 0
1
*
#-Intvl R-coord. (radial info.)
12111101 2
0.002655
*
comp-# interval-# (radial info.)
12111201 13
2
*
source value interval-# (radial info.)
12111301 0.0
2
*
initial temperature flag (if flag=0 or -1)
12111400 -1
*
temp-1 temp-2 temp-3
12111401 740.62 740.62 740.62
* L-B B.Vol.#
increment BC option surf.code area
NH
12111501 0
0
0
1
3.9581195 1 * Insula
* R-B B.Vol.#
increment BC option surf.code area
NH
12111601 211010000 10000
160
1
3.9581195 1
* Source source-type multiplier DHeat-Left DHeat-Right NH
12111701 0
0.
0.
0.
1
* Add R-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
12111901 0.0127 0.5 20. 0. 0. 0. 0. 1. 1
*
*
MATRIX CORE HEAT STRUCTURES: Average Channel (Plate)
*
#-HS #-MP geotype SS-ini L-coord.
12501000 8 8 1
0 0.0
*
mesh-loc format-flag
12501100 0
1
*
#-Intvl R-coord. (radial info.)
12501101 6
0.002355 * 1/2 fuel plate
12501102 1
0.002655 * coating thickn
*
comp-# interval-# (radial info.)
12501201 1
6 $ U02
12501202 -13
7 $ Ferritic SS
*
source interval-# (radial info.)
12501301 1.0
6
12501302 0.0
7
*
initial temperature flag (if flag=0
12501400 -1
*
temp. mesh point
12501401 934.97 934.24 932.06 928.42
899.31
12501402 1063.8 1062.8 1059.8 1054.8
1014.6
12501403 1172.9 1171.7 1168.1 1162.1
1114.0
12501404 1257.0 1255.8 1251.9 1245.4
1193.4
12501405 1311.0 1309.7 1305.8 1299.4
1247.5
119
reflood
bvol-ind axial#
dimension
dimension
or -1)
923.33
916.78
908.77
1047.8
1038.7
1027.7
1153.7
1142.9
1129.8
1236.4
1224.7
1210.5
1290.4
1278.8
1264.6
12501406 1332.3 1331.1 1327.5 1321.6 1313.3 1302.7 1289.6
1273.9
12501407 1321.2 1320.2 1317.2 1312.3 1305.4 1296.5 1285.6
1272.5
12501408 1280.3 1279.6 1277.4 1273.8 1268.9 1262.4 1254.6
1245.1
* L-B B.Vol.#
increment BC option surf.code surface area NH
12501501 0
0
0
1
107.159
8
* R-B B.Vol.#
increment BC option surf.code surface area NH
12501601 250010000 10000
160
1
107.159
8
** Source source-type multiplier DHeat-Left DHeat-Right NH
$ 1.25 chopped cosine shape $ He Core
12501701 1000 0.0844607 0.
0.
1
12501702 1000 0.1171673 0.
0.
2
12501703 1000 0.1405377 0.
0.
3
4
0.
12501704 1000 0.1527072 0.
12501705 1000 0.1527072 0.
0.
5
12501706 1000 0.1405377 0.
0.
6
12501707 1000 0.1171673 0.
0.
7
12501708 1000 0.0844607 0.
0.
8
*
12501900
* Add R-B
12501901
12501902
12501903
12501904
12501905
12501906
12501907
12501908
*
1
Dh HL-f
HL-r
0.0127 0.121875
0.0127 0.365625
0.0127 0.609375
0.0127 0.853125
0.0127 1.096875
0.0127 1.340625
0.0127 1.584375
0.0127 1.828125
grid-f
20. 0.
20. 0.
20. 0.
20.
0.
20. 0.
20.
0.
20.
0.
20.
0.
grid-r
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
grid-kf
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
grid-kr L-Boil
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
MATRIX CORE HEAT STRUCTURES: Hot Channel (Plate)
*
==*
#-HS #-MP geotype SS-ini L-coord.
*
12511000 8 8 1
0 0.00
*
mesh-loc format-flag
12511100 0
1
*
#-Intvl R-coord. (radial info.)
12511101 6
0.002355 * 1/2 fuel plate
0.002655 * coating thickn
12511102 1
comp-# interval-# (radial info.)
*
12511201 1
6 $ U02
7 $ Ferritic SS
12511202 -13
*
source interval-# (radial info.)
12511301 1.0
6
12511302 0.0
7
*
initial temperature flag (if flag=0
12511400 -1
temp. mesh point
*
12511401 968.50 967.67 965.17 960.99
927.57
12511402 1120.2 1119.0 1115.6 1109.8
1063.6
120
reflood
bvol-ind axial#
dimension
dimension
or -1)
955.15
947.64
938.45
1101.7
1091.4
1078.7
NH
1
2
3
4
5
6
7
8
12511403 1247.7 1246.4 1242.3 1235.4 1225.8 1213.5 1198.4
1180.3
12511404 1345.6 1344.1 1339.7 1332.3 1322.0 1308.7 1292.4
1272.7
12511405 1407.8 1406.4 1401.9 1394.6 1384.3 1371.0 1354.8
1335.1
12511406 1431.9 1430.6 1426.5 1419.8 1410.3 1398.1 1383.2
1365.1
12511407 1418.6 1417.5 1414.1 1408.5 1400.6 1390.4 1378.0
1362.9
12511408 1371.0 1370.2 1367.8 1363.7 1358.0 1350.6 1341.6
1330.8
* L-B B.Vol.#
increment BC option surf.code surface area NH
12511501 0
0
0
1
0.965395
8
* R-B B.Vol.#
increment BC option surf.code surface area NH
12511601 251010000 10000
160
1
0.965395
8
** Source source-type multiplier DHeat-Left DHeat-Right NH
$ 1.25 chopped cosine shape $ He Core
12511701 1000 0.0008750 0.
0.
1
12511702 1000 0.0012139 0.
0.
2
12511703 1000 0.0014560 0.
0.
3
12511704 1000 0.0015821 0.
0.
4
12511705 1000 0.0015821 0.
0.
5
12511706 1000 0.0014560 0.
0.
6
12511707 1000 0.0012139 0.
0.
7
12511708 1000 0.0008750 0.
0.
8
*
12511900
* Add R-B
12511901
12511902
12511903
12511904
12511905
12511906
12511907
12511908
1
Dh HL-f
HL-r
0.0127 0.121875
0.0127 0.365625
0.0127 0.609375
0.0127 0.853125
0.0127 1.096875
0.0127 1.340625
0.0127 1.584375
0.0127 1.828125
grid-f
20. 0.
20. 0.
20. 0.
20. 0.
20. 0.
20. 0.
20. 0.
20. 0.
grid-r
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
grid-kf
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
0. 1.
grid-kr L-Boil
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
0.0 1.1 1.0
*--------------------------------------------------------------*
*
*
reactor kinetics data
- ANS 79 Decay Heat Model used
*
*
*--------------------------------------------------------------*
30000000 point
separabl
30000001 gamma-ac 600.0e6 0.
30000002 ans79-1 200.0
30000011 100 * scram curve
* Density reactivity feedback
30000501 0.
0.0
30000502 1000. 0.0
30000601
*00.
0.0
30000601 13000.
0.0
30000602 3000.
0.0
* Doppler reactivity feedback
352.11268
1.0
*
* Volume weighting factor
*For
*
transient calculation, the following data should be used
For transient calculation, the following data should be used
121
NH
1
2
3
4
5
6
7
8
* instead of cards 30000801 - 820
* by SIL
*30000801
0.02365 -0.000859212
*300008012 1701001
0.031328 -0.000859212
*300008023 1701002
0.038502 -0.000997298
*300008034 1701003
0.045054 -0.000997298
1701004
*300008045
0.050881 -0.001072738
1701005
*300008056
1701006
0.055887 -0.001072738
*300008067
0.059993 -0.001072738
1701007
*300008078
1701008
0.063131 -0.001253016
*300008089
0.065252 -0.001253016
1701009
*30000809
0.066322 -0.001253016
1701010
*300008101
0.066322 -0.000722406
*300008112 1701011
0.065252 -0.000722406
*300008123 1701012
0.063131 -0.000722406
*300008134 1701013
0.059993 -0.000784413
*300008145 1701014
0.055887 -0.000784413
*300008156 1701015
0.050881 -0.000784413
1701016
*300008167
0.045054 -0.000746697
1701017
*300008178
0.038502 -0.000746697
1701018
*300008189
0.031328 -0.00052422
1701019
*3000081920
*3 000 082 0 1701020
0.02365 -0.00052422
*
---------------------------------*
~-~-'~i*n
*--
----------------------------------------------------------
*
*
20210000
20210001
20210002
20210003
20210004
20210005
20210006
20210007
20210008
20210009
20210010
*
reac-t
0.0
1.98
2.31
2.64
2.97
3.30
3.63
3.96
4.29
2.0e20
501
0.0
-0.052667
-0.158001
-0.421300
-0.974300
-2.212000
-4.371400
-5.029700
-5.266700
-5.266700
Lower Reflector-Entrance of Core Average Channel
#-HS #-MP geotype SS-ini L-coord. reflood
*
0 0.0
12901000 1 3 1
mesh-loc format-flag
*
1
12901100 0
#-Intvl R-coord. (radial info.)
*
0.002655
12901101 2
interval-# (radial info.)
comp-#
*
2
12901201 13
source value interval-# (radial info.)
*
2
12901301 0.0
initial temperature flag (if flag=0 or -1)
*
12901400 -1
temp-1 temp-2 temp-3
*
12901401 1105.6 1105.6 1105.6
122
(Plate)
bvol-ind axial#
* L-B
B.Vol.#
increment BC option surf.code area NH
12901501 0
0
0
1
439.62 1 * Zero hea
* R-B B.Vol.#
increment BC option surf.code area NH
12901601 290010000 10000
160
1
439.62 1
* Source source-type multiplier DHeat-Left DHeat-Right NH
12901701 0
0.
0.
0.
1
*
9-words format option
* Add R-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
12901901 0.0127 0.5 20. 0. 0. 0. 0. 1. 1
*
*
Lower Reflector-Entrance of Core Hot Channel (Plate)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
12911000 1 3 1
0 0.0
mesh-loc format-flag
*
12911100 0
1
*
#-Intvl R-coord. (radial info.)
12911101 2
0.002655
*
comp-# interval-# (radial info.)
12911201 13
2
*
source value interval-# (radial info.)
12911301 0.0
2
initial temperature flag (if flag=0 or -1)
*
12911400 -1
*
temp-i temp-2 temp-3
12911401 1168.8 1168.8 1168.8
* L-B B.Vol.#
increment BC option surf.code area
NH
12911501 0
0
0
1
3.9581195 1 * Zero
* R-B B.Vol.#
increment BC option surf.code area
NH
12911601 291010000 10000
160
1
3.9581195 1
* Source source-type multiplier DHeat-Left DHeat-Right NH
12911701 0
0.
0.
0.
1
* Add R-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
12911901 0.0127 0.5 20. 0. 0. 0. 0. 1. 1
*++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
++
*
**************************** STRUCTURE 5201
******************************
* Recuperator -- plate-fin
$
*ht str ht.strs m.pts
15201000 30
3 1 1
geom
0.0
init
0
l.coord
*
*
loc
15201100
flag
0
1
*
*
#
r
15201101 2
0.0004572
*
*
compos.
15201201 15
#
2
*
*
source #
15201301 0.0
2
123
refl
b.vol
ax.incr.
temperature flag
15201400 -1
*
temperature #
15201401 742.40
15201402 730.64
15201403 718.84
15201404 707.00
15201405 695.13
15201406 683.22
15201407 671.28
15201408 659.31
15201409 647.31
15201410 635.28
15201411 623.21
15201412 611.13
15201413 599.01
15201414 586.87
15201415 574.71
15201416 562.53
15201417 550.33
15201418 538.11
15201419 525.88
15201420 513.63
15201421 501.38
15201422 489.12
15201423 476.85
15201424 464.58
15201425 452.32
15201426 440.05
15201427 427.8
15201428 415.55
15201429 403.33
15201430 391.12
742.29
730.53
718.73
706.89
695.02
683.11
671.17
659.2
647.19
635.16
623.09
611.00
598.89
586.75
574.58
562.4
550.2
537.98
525.74
513.5
501.24
488.98
476.71
464.44
452.17
439.9
427.65
415.4
403.17
390.96
742.19
730.42
718.62
706.78
694.90
683.00
671.05
659.08
647.07
635.04
622.97
610.88
598.76
586.62
574.46
562.27
550.07
537.84
525.61
513.36
501.1
488.83
476.56
464.29
452.02
439.75
427.49
415.25
403.01
390.8
*
vol
15201501
inc
type code
520010000 10000
factor #
160
0 2192.0
30
*
vol
15201601
inc
type code
590300000 -10000
factor #
160
0 2192.0
30
*
type
15201701
mult D-lt D-rt # *source
0
0.0
0.0
0.0
30
15201800
*
Dhe
15201801
15201802
15201803
15201804
15201805
15201806
15201807
15201808
15201809
1
LHEf
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
LHEr LGSf LGSr Kfwd
0.047 2.768 10.0 10.0
0.141 2.674 10.0 10.0
0.235 2.581 10.0 10.0
0.328 2.487 10.0 10.0
0.422 2.393 10.0 10.0
0.516 2.299 10.0 10.0
0.610 2.205 10.0 10.0
0.704 2.111 10.0 10.0
0.798 2.018 10.0 10.0
124
Krev
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Fboil nclf povd
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
ff
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
15201810
15201811
15201812
15201813
15201814
15201815
15201816
15201817
15201818
15201819
15201820
15201821
15201822
15201823
15201824
15201825
15201826
15201827
15201828
15201829
15201830
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
2.7-4
0.891
0.985
1.079
1.173
1.267
1.361
1.455
1.548
1.642
1.736
1.830
1.924
2.018
2.111
2.205
2.299
2.393
2.487
2.581
2.674
2.768
15201900
*
Dhe
15201901
15201902
15201903
15201904
15201905
15201906
15201907
15201908
15201909
15201910
15201911
15201912
15201913
15201914
15201915
15201916
15201917
15201918
15201919
15201920
15201921
15201922
15201923
15201924
15201925
15201926
15201927
15201928
15201929
15201930
LHEf
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
2.4-4
LHEr LGSf LGSr Kfwd
2.768 0.047 10.0 10.0
2.674 0.141 10.0 10.0
2.581 0.235 10.0 10.0
2.487 0.328 10.0 10.0
2.393 0.422 10.0 10.0
2.299 0.516 10.0 10.0
2.205 0.610 10.0 10.0
2.111 0.704 10.0 10.0
2.018 0.798 10.0 10.0
1.924 0.891 10.0 10.0
1.830 0.985 10.0 10.0
1.736 1.079 10.0 10.0
1.642 1.173 10.0 10.0
1.548 1.267 10.0 10.0
1.455 1.361 10.0 10.0
1.361 1.455 10.0 10.0
1.267 1.548 10.0 10.0
1.173 1.642 10.0 10.0
1.079 1.736 10.0 10.0
0.985 1.830 10.0 10.0
0.891 1.924 10.0 10.0
0.798 2.018 10.0 10.0
0.704 2.111 10.0 10.0
0.610 2.205 10.0 10.0
0.516 2.299 10.0 10.0
0.422 2.393 10.0 10.0
0.328 2.487 10.0 10.0
0.235 2.581 10.0 10.0
0.141 2.674 10.0 10.0
0.047 2.768 10.0 10.0
1.924
1.830
1.736
1.642
1.548
1.455
1.361
1.267
1.173
1.079
0.985
0.891
0.798
0.704
0.610
0.516
0.422
0.328
0.235
0.141
0.047
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Krev
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Fboil nclf povd
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
0.0 1.0 2.815
**************************** COMPOSITION
125
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
2.815
1.0 1. 10
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
ff
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
15****************************
* thermal properties of GA design
* distortion in heatric pche
1
20101500 tbl/fctn
1
*----------------------------------------------------------------------
20101501
20101502
20101503
20101504
20101505
20101506
20101507
20101508
20101509
20101510
2.232611E+02
2.942611E+02
4.220389E+02
5.331500E+02
6.442611E+02
6.998167E+02
8.109278E+02
8.664833E+02
1.255372E+03
1.922039E+03
1.058900E+01
1.158900E+01
1.383203E+01
1.570122E+01
1.744581E+01
1.831810E+01
2.006268E+01
2.093497E+01
2.990710E+01
2.990710E+01
20101551
20101552
20101553
20101554
2.002611E+02
2.942611E+02
9.775944E+02
1.922039E+03
3.143784E+06
3.433784E+06
4.694627E+06
4.694627E+06
****************************
STRUCTURE 5301
* precooler -- tube/shell hx
$
*ht str ht.strs m.pts
5 2 1
15301000 20
geom init
0.0033 0
l.coord
refl
*
*
loc
15301100
flag
0
*
#
r
15301101 4
0.0045
*
compos.
*
15301201 16
*
*
source #
15301301 0.0
4
*
temperature flag
*
15301400 -1
*
*
temperature #
15301401 324.69
15301402 320.35
15301403 316.58
15301404 313.31
15301405 310.46
15301406 307.99
15301407 305.83
15301408 303.95
15301409 302.32
15301410 300.89
325.27
320.86
317.02
313.69
310.80
308.28
306.08
304.17
302.51
301.06
325.80
321.32
317.43
314.04
311.10
308.54
306.32
304.37
302.68
301.21
326.30
321.75
317.80
314.37
311.38
308.79
306.53
304.56
302.85
301.35
126
326.76
322.15
318.15
314.67
311.65
309.02
306.73
304.74
303.00
301.48
b.vol
ax.incr.
15301411
15301412
15301413
15301414
15301415
15301416
15301417
15301418
15301419
15301420
299.65
298.56
297.62
296.79
296.07
295.45
294.90
294.43
294.02
*
vol
15301501
inc
type code
133200000 -10000
factor
1
1
#
35500.
20
inc
type code
530010000 10000
factor
1
1
#
35500.
20
293.66
299.79
298.69
297.73
296.89
296.16
295.52
294.97
294.48
294.06
293.70
299.92
298.80
297.83
296.98
296.23
295.59
295.02
294.53
294.11
293.74
300.05
298.91
297.92
297.06
296.30
295.65
295.08
294.58
294.15
293.77
300.16
299.01
298.01
297.13
296.37
295.71
295.13
294.62
294.19
293.80
*
*
vol
15301601
*
*
type
15301701
mrult D-lt D-rt # *source
0
0.0
0.0
0.0
20
*
15301800
*
Dhe
15301801
15301802
15301803
15301804
15301805
15301806
15301807
15301808
15301809
15301810
15301811
15301812
15301813
15301814
15301815
15301816
15301817
15301818
15301819
15301820
1
LHEf LHEr LGSf LGSr Kfwd Krev
0.003394 4.612 0.118 10.0 10.0 0.0
0.003394 4.375 0.355 10.0 10.0 0.0
0.003394 4.139 0.591 10.0 10.0 0.0
0.003394 3 .902 0.828 10.0 10.0 0.0
0.003394 3.666 1.064 10.0 10.0 0.0
0.003394 3 .429 1.301 10.0 10.0 0.0
0.003394 3 .193 1.537 10.0 10.0 0.0
0.003394 2.956 1.774 10.0 10.0 0.0
0.003394 2.720 2 .010 10.0 10.0 0.0
0.003394 2 .483 2 .247 10.0 10.0 0.0
0.003394 2 .247 2 .483 10.0 10.0 0.0
0.003394 2 .010 2.720 10.0 10.0 0.0
0.003394 1.774 2 .956 10.0 10.0 0.0
0.003394 1.537 3 .193 10.0 10.0 0.0
0.003394 1.301 3.429 10.0 10.0 0.0
0.003394 1.064 3.666 10.0 10.0 0.0
0.003394 0.828 3 .902 10.0 10.0 0.0
0.003394 0.591 4.139 10.0 10.0 0.0
0.003394 0.355 4.375 10.0 10.0 0.0
0.003394 0.118 4 .612 10.0 10.0 0.0
Fboil nclf povd ff #
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
15301900
*
Dhe
15301901
15301902
15301903
15301904
15301905
15301906
15301907
15301908
15301909
15301910
15301911
1
LHEf LHEr LGSf LGSr Kfwd Krev
0.003394 0.118 4.612 10.0 10.0 0.0
0.003394 0.355 4.375 10.0 10.0 0.0
0.003394 0.591 4.139 10.0 10.0 0.0
0.003394 0.828 3.902 10.0 10.0 0.0
0.003394 1.064 3.666 10.0 10.0 0.0
0.003394 1.301 3.429 10.0 10.0 0.0
0.003394 1.537 3.193 10.0 10.0 0.0
0.003394 1.774 2.956 10.0 10.0 0.0
0.003394 2.010 2.720 10.0 10.0 0.0
0.003394 2.247 2.483 10.0 10.0 0.0
0.003394 2.483 2.247 10.0 10.0 0.0
Fboi 1lnclf povd ff #
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1 i1
127
1
15301912
15301913
15301914
15301915
15301916
15301917
15301918
15301919
15301920
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
2.720
2.956
3.193
3.429
3.666
3.902
4.139
4.375
4.612
2.010
1.774
1.537
1.301
1.064
0.828
0.591
0.355
0.118
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
12
13
14
15
16
17
18
19
20
*
*
**************************** COMPOSITION 16****************************
* thermal properties of ss-316 modified to compensate for volume
* distortion in heatric pche
20101600 tbl/fctn
1
* ss-316
1
*----------------------------------------------------------------------
20101601
20101602
20101603
20101604
20101605
20101606
283.15
310.93
533.15
699.82
810.93
1088.71
13.70
14.14
17.63
20.24
21.99
26.35
283.15
310.93
533.15
699.82
810.93
1088.71
3.115e06
3.237e06
3.733e06
3.865e06
3.958e06
4.309e06
*
20101651
20101652
20101653
20101654
20101655
20101656
* divided by 1.140
*
*
****************************
STRUCTURE 5701
************.**********.*****
* Inter-cooler -- tube/shell hx
$
*ht str ht.strs m.pts
5 2 1
15701000 20
geom init
0
0.0033
l.coord
refl
*
*
loc
15701100
flag
1
0
*
*
#
r
15701101 4
0.0045
*
*
compos.
15701201 16
#
4
*
*
source #
15701301 0.0
4
*
*
temperature flag
15701400 -1
*
*
temperature #
15701401 326.30 326.77
327.19
327.59
128
327.96
b.vol
ax.incr.
15701402
15701403
15701404
15701405
15701406
15701407
15701408
15701409
15701410
15701411
15701412
15701413
15701414
15701415
15701416
15701417
15701418
15701419
15701420
322.39
318.91
315.79
313.01
310.53
308.31
306.32
304.55
302.96
301.54
300.26
299.12
298.10
297.19
296.37
295.64
294.98
294.40
293.87
vol
15701501
inc
type code
143200000 -10000
factor
1
1
#
32000.
20
vol
15701601
inc
type code
570010000 10000
factor
1
1
#
32000.
20
type
15701701
mult D-lt D-rt # *source
20
0
0.0
0.0
0.0
*
*
*
322.81
319.28
316.13
313.31
310.80
308.55
306.54
304.74
303.13
301.69
300.40
299.25
298.21
297.29
296.46
295.72
295.06
294.46
293.93
323.19
319.62
316.43
313.58
311.04
308.77
306.73
304.92
303.29
301.83
300.53
299.36
298.31
297.38
296.54
295.79
295.12
294.52
293.98
323.55
319.94
316.71
313.84
311.27
308.97
306.92
305.08
303.43
301.96
300.64
299.46
298.41
297.46
296.62
295.86
295.18
294.57
294.03
323.87
320.23
316.98
314.07
311.48
309.16
307.09
305.23
303.57
302.08
300.75
299.56
298.50
297.54
296.69
295.92
295.24
294.62
294.07
*
15701800
*
Dhe
15701801
15701802
15701803
15701804
15701805
15701806
15701807
15701808
15701809
15701810
15701811
15701812
15701813
15701814
15701815
15701816
15701817
15701818
15701819
15701820
1
LHEf LHEr LGSf LGSr Kfwd Krev
0.003394 4.612 0.118 10.0 10.0 0.0
0.003394 4.375 0.355 10.0 10.0 0.0
0.003394 4.139 0.591 10.0 10.0 0.0
0.003394 3.902 0.828 10.0 10.0 0.0
0.003394 3.666 1.064 10.0 10.0 0.0
0.003394 3.429 1.301 10.0 10.0 0.0
0.003394 3.193 1.537 10.0 10.0 0.0
0.003394 2.956 1.774 10.0 10.0 0.0
0.003394 2.720 2.010 10.0 10.0 0.0
0.003394 2.483 2.247 10.0 10.0 0.0
0.003394 2.247 2.483 10.0 10.0 0.0
0.003394 2.010 2.720 10.0 10.0 0.0
0.003394 1.774 2.956 10.0 10.0 0.0
0.003394 1.537 3.193 10.0 10.0 0.0
0.003394 1.301 3.429 10.0 10.0 0.0
0.003394 1.064 3.666 10.0 10.0 0.0
0.003394 0.828 3.902 10.0 10.0 0.0
0.003394 0.591 4.139 10.0 10.0 0.0
0.003394 0.355 4.375 10.0 10.0 0.0
0.003394 0.118 4.612 10.0 10.0 0.0
Fboil nclf povd ff #
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
0.0 1.0 4.73 1.0 1.1
15701900 1
*
Dhe LHEf LHEr LGSf LGSr Kfwd Krev Fboil nclf povd ff #
15701901 0.003394 0.118 4.612 10.0 10.0 0.0 0.0 1.0 4.73 1.0 1.1
15701902 0.003394 0.355 4.375 10.0 10.0 0.0 0.0 1.0 4.73 1.0 1.1
129
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
1
2
15701903
15701904
15701905
15701906
15701907
15701908
15701909
15701910
15701911
15701912
15701913
15701914
15701915
15701916
15701917
15701918
15701919
15701920
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.003394
0.591
0.828
1.064
1.301
1.537
1.774
2.010
2.247
2.483
2.720
2.956
3.193
3.429
3.666
3.902
4.139
4.375
4.612
4.139
3.902
3.666
3.429
3.193
2.956
2.720
2.483
2.247
2.010
1.774
1.537
1.301
1.064
0.828
0.591
0.355
0.118
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
10.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
4.73
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
1.1
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
*
*
* Hot Leg Duct of Passive DHR System 1 (Cylinder):Wall Thickness
(0.027m)
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
*
0 0.575
16101000 5 3 2
*
mesh-loc format-flag
1
16101100 0
*
#-Intvl R-coord. (radial info.)
0.585
16101101 2
*
comp-# interval-# (radial info.)
2
16101201 6
*
source value interval-# (radial info.)
2
16101301 0.0
initial temperature flag (if flag=0 or -1)
*
16101400 -1
*
temp-i temp-2 temp-3
16101401 1095.9 1095.9 1095.9
16101402 1091.2 1091.2 1091.2
16101403 1090.3 1090.3 1090.3
16101404 1090.7 1090.7 1090.7
16101405 1093.8 1093.8 1093.8
* L-B B.Vol.# increment BC option surf.code height NH
2.60 5
1
160
16101501 610010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
2.60 5 * Insulate
1
0
0
16101601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
5
0.
0.
0.
16101701 0
9-words format option
*
16101800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16101801 1.150 1.3 20. 0. 0. 0. 0. 1. 1
16101802 1.150 3.9 20. 0. 0. 0. 0. 1. 2
16101803 1.150 6.5 20. 0. 0. 0. 0. 1. 3
130
16101804
16101805
* Add R-B
16101901
16101902
16101903
16101904
16101905
1.150 9.1 20.
1.150 11.7 20.
Dh HL-f HL-r
1.170 1.3 20.
1.170 3.9 20.
1.170 6.5 20.
1.170 9.1 20.
1.170 11.7 20.
0. 0.
0. 0.
grid-f
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
grid-r
0. 0.
0. 0.
0. 0.
0. 0.
0. 0.
1. 4
1. 5
grid-kf grid-kr L-Boil NH
1. 1
1. 2
1. 3
1. 4
1. 5
*
* Hot Leg Duct of Passive DHR System 2 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
16111000 5 3 2
0 0.575
*
mesh-loc format-flag
16111100 0
1
*
#-Intvl R-coord. (radial info.)
16111101 2
0.585
*
comp-# interval-# (radial info.)
16111201 6
2
*
source value interval-# (radial info.)
16111301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16111400 -1
*
temp-1 temp-2 temp-3
16111401 1084.7 1084.7 1084.7
16111402 1079.4 1079.4 1079.4
16111403 1071.3 1071.3 1071.3
16111404 1056.1 1056.1 1056.1
16111405 1023.9 1023.9 1023.9
* L-B B.Vol.#
increment BC option surf.code height NH
16111501 611010000 10000
160
1
2.60 5
* R-B B.Vol.#
increment BC option surf.code height NH
16111601 0
0
0
1
2.60 5 * Insulated
* Source source-type multiplier DHeat-Left DHeat-Right NH
16111701 0
0.
0.
0.
5
*
9-words format option
16111800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16111801 1.150 1.3 20. 0. 0. 0. 0. 1. 1
16111802 1.150 3.9 20. 0. 0. 0. 0. 1. 2
16111803 1.150 6.5 20. 0. 0. 0. 0. 1. 3
16111804 1.150 9.1 20. 0. 0. 0. 0. 1. 4
16111805 1.150 11.7 20. 0. 0. 0. 0. 1. 5
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16111901 1.170 1.3 20. 0. 0. 0. 0. 1. 1
16111902 1.170 3.9 20. 0. 0. 0. 0. 1. 2
16111903 1.170 6.5 20. 0. 0. 0. 0. 1. 3
16111904 1.170 9.1 20. 0. 0. 0. 0. 1. 4
16111905 1.170 11.7 20. 0. 0. 0. 0. 1. 5
*
*====
==
-
-
-= ====
===
===
====
===
===
131
=-=-
-=-
-
-
-
-
-
-
-
- ==-
--===
* HX pod Inlet of Passive DHR System 1 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
16201000 1 3 2
0 0.818
*
mesh-loc format-flag
1
16201100 0
*
#-Intvl R-coord. (radial info.)
16201101 2
0.828
*
comp-# interval-# (radial info.)
16201201 6
2
*
source value interval-# (radial info.)
16201301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16201400 -1
*
temp-1 temp-2 temp-3
16201401 1118.6 1118.6 1118.6
increment BC option surf.code height NH
* L-B B.Vol.#
160
1
4.50 1
16201501 620010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
16201601 0
0
0
1
4.50 1 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
1
0.
0.
16201701 0
*
9-words format option
16201800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16201801 1.636 2.25 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16201901 1.656 2.25 20. 0. 0. 0. 0. 1. 1
*
* HX pod Inlet of Passive DHR System 2 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 0.818
16211000 1 3 2
*
mesh-loc format-flag
1
16211100 0
*
#-Intvl R-coord. (radial info.)
0.828
16211101 2
comp-# interval-# (radial info.)
*
2
16211201 6
*
source value interval-# (radial info.)
2
16211301 0.0
*
initial temperature flag (if flag=0 or -1)
16211400 -1
*
temp-i temp-2 temp-3
16211401 932.43 932.43 932.43
* L-B B.Vol.# increment BC option surf.code height NH
160
1
4.50 1
16211501 621010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
1
4.50 1 * Insulate
0
0
16211601 0
132
* Source source-type multiplier DHeat-Left DHeat-Right NH
16211701 0
0.
0.
0.
1
*
9-words format option
16211800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16211801 1.636 2.25 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16211901 1.656 2.25 20. 0. 0. 0. 0. 1. 1
*
*
HX Inlet of Passive DHR System 1 (Cylinder):Wall Thickness (0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
16261000 1 3 2
0 0.075
*
mesh-loc format-flag
16261100 0
1
*
#-Intvl R-coord. (radial info.)
16261101 2
0.085
*
comp-# interval-# (radial info.)
16261201 6
2
*
source value interval-# (radial info.)
16261301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16261400 -1
*
temp-i temp-2 temp-3
16261401 1086.5 1086.5 1086.5
* L-B B.Vol.# increment BC option surf.code height NH
16261501 626010000 10000
160
1
1.00 1
* R-B B.Vol.# increment BC option surf.code height NH
16261601 0
0
1.00 1 * Insulate
0
1
* Source source-type multiplier DHeat-Left DHeat-Right NH
16261701 0
0.
0.
0.
1
*
9-words format option
16261800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16261801 0.150 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16261901 0.170 0.50 20. 0. 0. 0. 0. 1. 1
*
*
*---
HX Inlet of Passive DHR System 2 (Cylinder):Wall Thickness (0.027m)
-
-
-
-
-
-
-
-
-
-
*
#-HS #-MP geotype SS-ini L-coord. reflood
16291000 1 3 2
0 0.075
*
mesh-loc format-flag
16291100 0
1
*
#-Intvl R-coord. (radial info.)
16291101 2
0.085
*
comp-# interval-# (radial info.)
133
-
-
-
-
-
bvol-ind axial#
-
16291201 6
2
source value interval-# (radial info.)
*
2
16291301 0.0
*
initial temperature flag (if flag=0 or -1)
16291400 -1
temp-1 temp-2 temp-3
*
16291401 372.51 372.51 372.51
* L-B B.Vol.#
increment BC option surf.code height NH
1.00 1
160
1
16291501 629010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
0
0
1
1.00 1 * Insulate
16291601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
0.
1
0.
16291701 0
*
9-words format option
16291800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16291801 0.150 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16291901 0.170 0.50 20. 0. 0. 0. 0. 1. 1
*Passive
DHR HEAT EXCHANGER
1
Passive DHR HEAT EXCHANGER
1
*
*
*
*====
===
====
===
===
====
===
===
====
===
====
===
===
====
===
===
*---------------------------------------------------------
*
Heat Exchanger (model in cylindrical coord)
*---------------------------------------------------------
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 1.5275e-3
16501000 5 3 1
*
mesh-loc format-flag
16501100 0
1
*
#-Intvl R-coord. (radial info.)
3.0275e-3
16501101 2
comp-# interval-# (radial info.)
*
16501201 6
2
*
source value interval-# (radial info.)
2
16501301 0.0
*
initial temperature flag (if flag=0 or -1)
16501400 -1
*
temp. mesh point temp. mesh point
16501401 298.01 298.01 298.01
16501402 298.01 298.01 298.01
16501403 298.01 298.01 298.01
16501404 298.00 298.00 298.00
16501405 298.00 298.00 298.00
increment BC option surf.code surf area NH *H=#of
* L-B B.Vol.#
1
53.62
5 *139050
160
16501501 650010000 10000
increment BC option surf.code surf area NH
* R-B B.Vol.#
53.62
5
160
1
16501601 710050000 -10000
4171.5 5 *tempera
0
1401
1
*16501601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
134
0
0.
0.
0.
5
Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
3.0550e-3 0.03 20. 0. 0.
0. 0.
1. 1
3.0550e-3 0.09 20. 0. 0.
0. 0.
1. 2
0. 0.
3.0550e-3 0.15 20. 0. 0.
1. 3
3.0550e-3 0.21 20. 0. 0.
0.
0.
1. 4
3.0550e-3 0.27 20. 0. 0.
0. 0.
1. 5
Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
3.0550e-3 0.03 20. 0. 0.
0. 0.
1. 1
3.0550e-3 0.09 20. 0. 0.
1. 2
0. 0.
3.0550e-3 0.15 20. 0. 0.
0. 0.
1. 3
3.0550e-3 0.21 20. 0. 0.
0. 0.
1. 4
3.0550e-3 0.27 20. 0. 0.
0. 0.
1. 5
16501701
* Add L-B
16501801
16501802
16501803
16501804
16501805
* Add R-B
16501901
16501902
16501903
16501904
16501905
*------------------------------------
*
Passive DHR HEAT EXCHANGER
2
*
*-
-
-
-
-
-
-
-
-
*---------------------------
*
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
==
- ===
-
- ===
-
- ===-
- ===-
-- ===
-----------------------------
Heat Exchanger
*---------------------------------------------------------
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
16511000 5
3 1
0 1.5275e-3
*
mesh-loc format-flag
16511100 0
1
*
#-Intvl R-coord. (radial info.)
16511101 2
3.0275e-3
*
comp-# interval-# (radial info.)
16511201 6
2
source value interval-# (radial info.)
*
16511301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16511400 -1
*
temp. mesh point temp. mesh point
16511401 298.01 298.01 298.01
16511402 298.01 298.01 298.01
16511403 298.01 298.01 298.01
16511404 298.00 298.00 298.00
16511405 298.00 298.00 298.00
* L-B B.Vol.# increment BC option surf.code surf area NH
16511501 651010000 10000
160
1
53.62
5
* R-B B.Vol.# increment BC option surf.code surf area NH
16511601 711050000 -10000
160
1
53.62
5
*16511601 0
0
1401
1
4171.5
5 *te
* Source source-type multiplier DHeat-Left DHeat-Right NH
16511701 0
0.
0.
0.
5
* Add L-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil
16511801 3.0550e-3 0.03 20. 0. 0. 0. 0. 1. 1
16511802 3.0550e-3 0.09 20. 0. 0. 0. 0. 1. 2
16511803 3.0550e-3 0.15 20. 0. 0. 0. 0. 1. 3
16511804 3.0550e-3 0.21 20. 0. 0. 0. 0. 1. 4
16511805 3.0550e-3 0.27 20. 0. 0. 0. 0. 1. 5
* Add R-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil
16511901 3.0550e-3 0.03 20. 0. 0. 0. 0. 1. 1
135
NH
NH
16511902
16511903
16511904
16511905
3.0550e-3
3.0550e-3
3.0550e-3
3.0550e-3
0.09
0.15
0.21
0.27
20.
20.
20.
20.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1.
1.
1.
1.
2
3
4
5
*
*
HX Outlet of Passive DHR System 1 (Cylinder):Wall Thickness (0.027m)
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
*
0 0.075
16601000 1 3 2
*
mesh-loc format-flag
1
16601100 0
#-Intvl R-coord. (radial info.)
*
0.085
16601101 2
*
comp-# interval-# (radial info.)
16601201 6
2
*
source value interval-# (radial info.)
16601301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16601400 -1
temp-i temp-2 temp-3
*
16601401 607.58 607.58 607.58
increment BC option surf.code height NH
* L-B B.Vol.#
1
1.00 1
160
16601501 660010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
1
1.00 1 * Insulate
0
0
16601601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
1
0.
0.
16601701 0
*
9-words format option
16601800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16601801 0.150 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16601901 0.170 0.50 20. 0. 0. 0. 0. 1. 1
*
*
HX Outlet of Passive DHR System 2 (Cylinder):Wall Thickness (0.027m)
#-HS #-MP geotype SS-ini L-coord. reflood
*
0 0.075
16681000 1 3 2
*
mesh-loc format-flag
1
16681100 0
#-Intvl R-coord. (radial info.)
*
0.085
16681101 2
*
comp-# interval-# (radial info.)
2
16681201 6
source value interval-# (radial info.)
*
2
16681301 0.0
initial temperature flag (if flag=0 or -1)
*
16681400 -1
*
temp-1 temp-2 temp-3
136
bvol-ind axial#
16681401 503.73 503.73 503.73
* L-B B.Vol.#
increment BC option surf.code height NH
16681501 668010000 10000
160
1
1.00 1
* R-B B.Vol.#
increment BC option surf.code height NH
16681601 0
0
0
1.00 1 * Insulate
1
* Source source-type multiplier DHeat-Left DHeat-Right NH
16681701 0
0.
0.
0.
1
*
9-words format option
16681800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16681801 0.150 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16681901 0.170 0.50 20. 0. 0. 0. 0. 1. 1
*
-
.*----
-
-
-
-
-
-
--
-
-
-
-
-
-
-
* HX Outlet Pod of Passive DHR System 1 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
16621000 1 3 2
0 1.013
*
mesh-loc format-flag
16621100 0
1
*
#-Intvl R-coord. (radial info.)
16621101 2
1.023
*
comp-# interval-# (radial info.)
16621201 6
2
*
source value interval-# (radial info.)
16621301 0.0
2
*
initial temperature flag (if flag=0 or -1)
16621400 -1
temp-i temp-2 temp-3
*
16621401 751.45 751.45 751.45
* L-B B.Vol.#
increment BC option surf.code height NH
16621501 662010000 10000
160
1
1.00 1
* R-B B.Vol.#
increment BC option surf.code height NH
16621601 0
0
0
1
1.00 1 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
16621701 0
0.
0.
0.
1
*
9-words format option
16621800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16621801 2.026 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16621901 2.046 0.50 20. 0. 0. 0. 0. 1. 1
*
* HX Outlet Pod of Passive DHR System 2 (Cylinder):Wall Thickness
(0.027m)
*=====
====
-====
====
-===
=
-=
-
137
-==-=-
-
-
-
-
- ====
-
-
-
-
--
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 1.013
16711000 1 3 2
*
mesh-loc format-flag
1
16711100 0
*
#-Intvl R-coord. (radial info.)
16711101 2
1.023
comp-# interval-# (radial info.)
*
16711201 6
2
source value interval-# (radial info.)
*
2
16711301 0.0
*
initial temperature flag (if flag=0 or -1)
16711400 -1
temp-3
*
temp-1 temp-2
16711401 514.68 514.68 514.68
* L-B B.Vol.#
increment BC option surf.code height NH
16711501 671010000 10000
160
1
1.00 1
increment BC option surf.code height NH
* R-B B.Vol.#
1
1.00 1 * Insulate
0
0
16711601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
1
0.
0.
0.
16711701 0
9-words format option
*
16711800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16711801 2.026 0.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
0. 0. 0. 0. 1. 1
16711901 2.046 0.50 20.
*
* Blower Volume of Passive DHR System 1 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 0.7
16641000 1 3 2
*
mesh-loc format-flag
1
16641100 0
*
#-Intvl R-coord. (radial info.)
0.71
16641101 2
*
comp-# interval-# (radial info.)
2
16641201 6
*
source value interval-# (radial info.)
2
16641301 0.0
*
initial temperature flag (if flag=0 or -1)
16641400 -1
*
temp-i temp-2 temp-3
16641401 755.72 755.72 755.72
increment BC option surf.code height NH
* L-B B.Vol.#
1
3.00 1
160
16641501 664010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
3.00 1 * Insulate
1
0
0
16641601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
1
0.
0.
0.
16641701 0
9-words format option
*
138
16641800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16641801 1.400 1.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16641901 1.420 1.50 20. 0. 0. 0. 0. 1. 1
*
* Blower Volume of Passive DHR System 2 (Cylinder):Wall Thickness
(0.027m)
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 0.7
16731000 1 3 2
mesh-loc format-flag
*
16731100 0
1
*
#-Intvl R-coord. (radial info.)
0.71
16731101 2
*
comp-# interval-# (radial info.)
16731201 6
2
*
source value interval-# (radial info.)
2
16731301 0.0
*
initial temperature flag (if flag=0 or -1)
16731400 -1
*
temp-i temp-2 temp-3
16731401 533.78 533.78 533.78
* L-B B.Vol.#
increment BC option surf.code height NH
16731501 673010000 10000
160
1
3.00 1
* R-B B.Vol.#
increment BC option surf.code height NH
16731601 0
0
0
1
3.00 1 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
16731701 0
0.
0.
0.
1
*
9-words format option
16731800 0 *This 9-words format excludes the pitch-to-diameter ratio
on 801* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16731801 1.400 1.50 20. 0. 0. 0. 0. 1. 1
*
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16731901 1.420 1.50 20. 0. 0. 0. 0. 1. 1
*
*
Cold Leg Duct of Passive DHR System 1 (Cylinder)
*
#-HS #-MP geotype SS-ini L-coord. reflood
16661000 5 5 2
0 0.76
*
mesh-loc format-flag
1
16661100 0
*
#-Intvl R-coord. (radial info.)
16661101 4
0.79
*
comp-# interval-# (radial info.)
16661201 6
4
*
source value interval-# (radial info.)
16661301 0.0
4
*
initial temperature flag (if flag=0 or -1)
139
bvol-ind axial#
16661400 -1
temp-i temp-2 temp-3 temp-4 temp-5
*
717.70
717.70
717.70
717.70
16661401 717.70
717.70
717.70
717.70
717.70
16661402 717.70
717.70
717.70
717.70
717.70
16661403 717.70
717.70
717.70
717.70
717.70
16661404 717.70
717.70
717.70
717.70
717.70
16661405 717.70
increment BC option surf.code height NH
* L-B B.Vol.#
12.50 5
160
1
16661501 666010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
0
1
12.50 5 * Insulate
0
16661601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
5
0.
0.
0.
16661701 0
*
9-words format option
16661800 0
* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
16661801 1.520 1.25 20. 0. 0. 0. 0. 1. 1
16661802 1.520 3.75 20. 0. 0. 0. 0. 1. 2
16661803 1.520 6.25 20. 0. 0. 0. 0. 1. 3
16661804 1.520 8.75 20. 0. 0. 0. 0. 1. 4
16661805 1.520 11.25 20. 0. 0. 0. 0. 1. 5
* Add R-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
0. 0. 0. 0. 1. 1
16661901 1.580 1.25 20.
16661902 1.580 3.75 20. 0. 0. 0. 0. 1. 2
16661903 1.580 6.25 20. 0. 0. 0. 0. 1. 3
0. 0. 0. 0. 1. 4
16661904 1.580 8.75 20.
16661905 1.580 11.25 20. 0. 0. 0. 0. 1. 5
*
*
Cold Leg Duct of Passive DHR System 2 (Cylinder)
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
*
0 0.76
16761000 5 5 2
*
mesh-loc format-flag
1
16761100 0
*
#-Intvl R-coord. (radial info.)
0.79
16761101. 4
comp-# interval-# (radial info.)
*
4
16761201 6
source value interval-# (radial info.)
*
4
16761301 0.0
*
initial temperature flag (if flag=0 or -1)
16761400 -1
*
temp-i temp-2 temp-3 temp-4 temp-5
717.70
717.70
717.70
717.70
16761401 717.70
717.70
717.70
717.70
717.70
16761402 717.70
717.70
717.70
717.70
717.70
16761403 717.70
717.70
717.70
717.70
717.70
16761404 717.70
717.70
717.70
717.70
717.70
16761405 717.70
increment BC option surf.code height NH
* L-B B.Vol.#
2.50 5
1
160
16761501 676010000 10000
increment BC option surf.code height NH
* R-B B.Vol.#
1
2.50 5 * Insulated
0
0
16761601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
5
0.
0.
0.
16761701 0
9-words format option
*
16761800 0
140
* Add L-B
16761801
16761802
16761803
16761804
16761805
* Add R-B
16761901
16761902
16761903
16761904
16761905
Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
1.520 1.25 20. 0. 0. 0. 0. 1. 1
1.520 3.75 20.
0. 0. 0. 0. 1. 2
1.520 6.25 20. 0. 0. 0. 0. 1. 3
1.520 8.75 20. 0. 0. 0. 0. 1. 4
1.520 11.25 20. 0. 0. 0. 0. 1. 5
Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
1.580 1.25 20. 0. 0. 0. 0. 1. 1
1.580 3.75 20. 0. 0. 0. 0. 1. 2
1.580 6.25 20. 0. 0. 0. 0. 1. 3
1.580 8.75 20. 0. 0. 0. 0. 1. 4
1.580 11.25 20. 0. 0. 0. 0. 1. 5
*
*
Passive UHS DHR HEAT EXCHANGER
1
*
-
*--------------------------------------------*
*
Heat Exchanger
*---------------------------------------------------------
*
#-HS #-MP geotype SS-ini L-coord. reflood
17501000 20 5 2
0 1.7526e-2
*
mesh-loc format-flag
17501100 0
1
*
#-Intvl R-coord. (radial info.)
17501101 4
2.0182e-2
*
comp-# interval-# (radial info.)
17501201 6
4
source value interval-# (radial info.)
*
17501301 0.0
4
*
initial temperature flag (if flag=0 or -1)
17501400 -1
*
temp. mesh point temp. mesh point
17501401 298.00 298.00 298.00 298.00 298.00
17501402 298.00 298.00 298.00 298.00 298.00
17501403 298.00 298.00 298.00 298.00 298.00
17501404 298.00 298.00 298.00 298.00 298.00
17501405 298.00 298.00 298.00 298.00 298.00
17501406 298.00 298.00 298.00 298.00 298.00
17501407 298.00 298.00 298.00 298.00 298.00
17501408 298.00 298.00 298.00 298.00 298.00
17501409 298.00 298.00 298.00 298.00 298.00
17501410 298.00 298.00 298.00 298.00 298.00
17501411 298.00 298.00 298.00 298.00 298.00
17501412 298.00 298.00 298.00 298.00 298.00
17501413 298.00 298.00 298.00 298.00 298.00
17501414 298.00 298.00 298.00 298.00 298.00
17501415 298.00 298.00 298.00 298.00 298.00
17501416 298.00 298.00 298.00 298.00 298.00
17501417 298.00 298.00 298.00 298.00 298.00
17501418 298.00 298.00 298.00 298.00 298.00
17501419 298.00 298.00 298.00 298.00 298.00
17501420 298.00 298.00 298.00 298.00 298.00
141
bvol-ind axial#
increment BC option surf.code height NH
* L-B B.Vol.#
160.5 20
1
160
17501501 750010000 10000
Height NH
surf.code
option
BC
increment
B.Vol.#
R-B
*
*temperature
20
160.5
1
1401
0
17501601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
20
0.
0.
0.
17501701 0
* Add L-B
Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
1. 1
0.
0.
0.
0.
17501801 3.5052e-2 0.08025el 20.
1.
2
0.
0 . 0.
0 .24075e1 20. 0.
17501802 3. 5052e-2
1.
3
.
0.
0.
0 .40125e1 20. 0.
3 .5052e-2
17501803
1.
4
0. .
0.
20.
0 .56175e1
0.
3 .5052e-2
17501804
ci
1.
5
r
0.
.
0.
0 .72225e1 20. 0.
17501805 3 5052e-2
1.
6
0.
.
0.
20.
0.
0 .88275e1
17501806 3.5052e-2
1.
7
.
0.
0.
20.
.04325e1
1
0.
17501807 3 .5052e-2
1.
8
I
20.
.
0.
0.
.20375e1
0.
17501808 3.5052e-2
rc
1.
9
0.
20.
0.
.36425e1
).
1
0.
.5052e-2
3
17501809
c
1.
10
c. 0.
0.
0.
17501810 3.5052e-2 1 .52475e1 20.
1.
11
c. 0.
0.
0.
17501811 3.5052e-2 1 .68525e1 20.
1.
12
0.
0.
0.
0.
3 .5052e-2 1 .84575e1 20.
17501812
2
1.
13
0.
c. 0.
.00625e1 20. 0.
17501813 3 .5052e-2
2
1.
14
0.
0.
0.
.16675e1 20. 0.
17501814 3.5052e-2
2
1.
15
0.
0.
.32725e1 20. 0.
0.
17501815 3 .5052e-2
2
1.
16
20.
0.
0.
0.
.48775e1
0.
17501816 3 .5052e-2
1.
17
0.
20.
0.
0.
2.64825e1
0.
17501817 3.5052e-2
1.
18
0.
0.
0.
20.
2.80875e1
0.
17501818 3 .5052e-2
1.
19
20.
0.
0.
0.
2.96925e1
0.
5052e-2
3.
17501819
1.
20
0.
0.
0.
0.
3 .5052e-2 3.12975e1 20.
17501820
grid-kf grid- kr L-Boil NH
HL-r grid-f
grid r
* Add R-B Dh HL-f
1.
1
0.
0.
0.
0.08025e1 20. 0.
17501901 4. 0364e-2
1.
2
0.
0.
0.
0.24075e1 20. 0.
17501902 4. 0364e-2
1.
3
0.
0.
0.
0.40125e1 20. 0.
17501903 4.0364e-2
1.
4
20.
0.
0.
0.
0.
17501904 4. 0364e-2 0.56175e1
1.
5
0.
0.
0.
20.
0.
17501905 4. 0364e-2 0.72225e1
1.
6
0.
20.
0.
0.
0.88275e1
0.
4. 0364e-2
17501906
1.
7
0.
20.
0.
0.
1.04325e1
0.
4.
0364e-2
17501907
1.
8
20.
0.
0.
0.
1.20375e1
0.
4.0364e-2
17501908
1.
9
0.
0.
0.
4. 0364e-2 1.36425e1 20. 0.
17501909
1.
10
0.
0.
0.
4.0364e-2 1.52475e1 20. 0.
17501910
1.
11
0.
0.
0.
17501911 4.0364e-2 1.68525e1 20. 0.
1.
12
0.
0.
0.
17501912 4.0364e-2 1.84575e1 20. 0.
1.
13
0.
0.
0.
17501913 4.0364e-2 2.00625e1 20. 0.
1.
14
0.
0.
0.
20.
0.
4.0364e-2 2.16675e1
17501914
1.
15
0.
0.
0.
20.
2.32725e1
0.
17501915 4.0364e-2
1.
16
0.
0.
0.
20.
2.48775e1
0.
17501916 4.0364e-2
1.
17
0.
0.
0.
20.
2.64825e1
0.
4.0364e-2
17501917
1.
18
0.
0.
0.
20.
2.80875e1
0.
4.0364e-2
17501918
1.
19
0.
0.
0.
0.
17501919 4.0364e-2 2.96925e1 20.
1.
20
0.
0.
0.
3.12975e1 20.
0.
4.0364e-2
17501920
C
O
*
*
Passive UHS DHR HEAT EXCHANGER
2
*
*
142
*
Heat Exchanger
--------------------------------------------
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
0 1.7526e-2
17511000 20 5 2
*
mesh-loc format-flag
17511100 0
1
*
#-Intvl R-coord. (radial info.)
2.0182e-2
17511101 4
*
comp-# interval-# (radial info.)
17511201 6
4
*
source value interval-# (radial info.)
17511301 0.0
4
*
initial temperature flag (if flag=0 or -1)
17511400 -1
*
temp. mesh point temp. mesh point
17511401 298.00 298.00 298.00 298.00 298.00
17511402 298.00 298.00 298.00 298.00 298.00
17511403 298.00 298.00 298.00 298.00 298.00
17511404 298.00 298.00 298.00 298.00 298.00
17511405 298.00 298.00 298.00 298.00 298.00
17511406 298.00 298.00 298.00 298.00 298.00
17511407 298.00 298.00 298.00 298.00 298.00
17511408 298.00 298.00 298.00 298.00 298.00
17511409 298.00 298.00 298.00 298.00 298.00
17511410 298.00 298.00 298.00 298.00 298.00
17511411 298.00 298.00 298.00 298.00 298.00
17511412 298.00 298.00 298.00 298.00 298.00
17511413 298.00 298.00 298.00 298.00 298.00
17511414 298.00 298.00 298.00 298.00 298.00
17511415 298.00 298.00 298.00 298.00 298.00
17511416 298.00 298.00 298.00 298.00 298.00
17511417 298.00 298.00 298.00 298.00 298.00
17511418 298.00 298.00 298.00 298.00 298.00
17511419 298.00 298.00 298.00 298.00 298.00
17511420 298.00 298.00 298.00 298.00 298.00
* L-B B.Vol.# increment BC option surf.code height NH
17511501 751010000 10000
160
1
160.5 20
* R-B B.Vol.#
increment BC option surf.code height NH
17511601 0
0
1401
1
160.5 20 *temperatu
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
0.
0.
20
17511701
* Add L-B Dh
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
17511801 3.5052e-2
0.08025e1 20.
0. 0. 0. 0. 1. 1
17511802 3.5052e-2 0.24075e1 20. 0.
0. 0. 0.
1. 2
17511803 3.5052e-2
0.40125e1 20.
0. 0. 0. 0. 1. 3
17511804 3.5052e-2 0.56175e1 20.
0. 0. 0. 0. 1. 4
17511805 3. 5052e-2
0.72225el 20.
0. 0. 0. 0. 1. 5
17511806 3. 5052e-2
0.88275e1 20.
0. 0. 0. 0. 1.
6
17511807 3. 5052e-2
1.04325e1 20.
0. 0. 0. 0. 1. 7
17511808 3.5052e-2
1.20375e1 20.
0. 0. 0. 0. 1.
8
17511809 3. 5052e-2
1.36425e1 20.
0. 0. 0. 0.
1. 9
17511810 3. 5052e-2
1.52475e1 20.
0. 0. 0. 0. 1. 10
17511811 3. 5052e-2
1.68525e1 20.
0. 0. 0. 0.
1. 11
17511812 3. 5052e-2
1.84575e1 20.
0. 0. 0. 0. 1. 12
17511813 3. 5052e-2
2.00625el 20.
0.
0. 0. 0. 1.
13
17511814 3. 5052e-2
2.16675e1 20.
0. 0. 0. 0. 1. 14
17511815 3.5052e-2
2.32725el 20.
0. 0. 0. 0. 1. 15
143
17511816
17511817
17511818
17511819
17511820
* Add R-B
17511901
17511902
17511903
17511904
17511905
17511906
17511907
17511908
17511909
17511910
17511911
17511912
17511913
17511914
17511915
17511916
17511917
17511918
17511919
17511920
3.5052e-2 2.48775e1 20.
3.5052e-2 2.64825e1 20.
3.5052e-2 2.80875e1 20.
3.5052e-2 2.96925e1 20.
3.5052e-2 3.12975e1 20.
Dh
HL- f HL-r gri d-f
4.0364e-2 0.08025e1 20.
4.0364e-2 0.24075e1 20.
4.0364e-2 0.40125e1 20.
4.0364e-2 0.56175e1 20.
4.0364e-2 0.72225e1 20.
4.0364e-2 0.88275e1 20.
4.0364e-2 1.04325e1 20.
4.0364e-2 1.20375el 20.
4.0364e-2 1.36425e1 20.
4.0364e-2 1.52475e1 20.
4.0364e-2 1.68525e1 20.
4.0364e-2 1.84575e1 20.
4.0364e-2 2.00625e1 20.
4.0364e-2 2.16675e1 20.
4.0364e-2 2.32725e1 20.
4.0364e-2 2.48775e1 20.
4.0364e-2 2.64825e1 20.
2.80875e1 20.
4.0364e-2
2.96925e1 20.
4.0364e-2
3.12975e1 20.
4. 0364e-2
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
grid-r
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
grid-kf
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1.
16
1. 17
1. 18
1. 19
1. 20
grid-kr L-Boil NH
1. 1
1. 2
1. 3
1. 4
1. 5
1. 6
1. 7
1. 8
1. 9
1. 10
1. 11
1. 12
1. 13
1. 14
1. 15
1. 16
1. 17
1. 18
1. 19
1. 20
*---------------------------------------------
* General
*
time
20240100
20240101
20240102
*
Table for Surface Temperature of HX
tempature
temp
298.00
0.0
1.e5 298.00
Containment Ferrit SS perimeter
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
*
0 15.0
10701000 1 7 2
mesh-loc format-flag
*
1
10701100 0
#-Intvl R-coord. (radial info.)
*
15.025
10701101 2
15.225
10701102 4
comp-# interval-# (radial info.)
*
2
10701201 17
6
10701202 6
source value interval-# (radial info.)
*
6
10701301 0.0
initial temperature flag (if flag=0 or -1)
*
10701400 -1
temp-i temp-2 temp-3
*
10701401 303.15 303.15 303.15 303.15 303.15 303.15 303.15
increment BC option surf.code height NH
* L-B B.Vol.#
25.0 1
1
160
10701501 070010000 10000
144
* R-B B.Vol.#
increment BC option surf.code height NH
10701601 0
0
0
1
25.0 1 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
10701701 0
0.
0.
0.
1
*
10701800 1 *This 12-words format
* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
10701801 0.0 15. 15. 0. 0. 0. 0. 1. 0. 1.1 1.0 1
*
* Add R-B Dh
10701901 0.0
HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
15.
15.
0. 0. 0. 0. 1. 1
*
*
Containment Concrete floor
*
#-HS #-MP geotype SS-ini L-coord. reflood bvol-ind axial#
10702000 1 5 1
0 15.0
*
mesh-loc format-flag
10702100 0
1
*
#-Intvl R-coord. (radial info.)
10702101 4
15.5
*
comp-# interval-# (radial info.)
10702201 14
4
source value interval-# (radial info.)
*
10702301 0.0
4
*
initial temperature flag (if flag=0 or -1)
10702400 -1
*
temp-1 temp-2 temp-3
10702401 303.15 303.15 303.15 303.15 303.15
* L-B B.Vol.#
increment BC option surf.code height NH
10702501 070010000 10000
131
0
700. 1
* R-B B.Vol.# increment BC option surf.code height NH
10702601 0
0
0
0
700.0 1 * Insulate
* Source source-type multiplier DHeat-Left DHeat-Right NH
10702701 0
0.
0.
0.
1
*
10702800 1 *This 12-words format
* Add L-B Dh HL-f HL-r grid-f grid-r
10702801 48.51 15. 15. 0. 0. 0. 0.
grid-kf grid-kr L-Boil NH
1. 0. 1.1 1.0 1
*
* Add R-B Dh HL-f HL-r
10702901 48.51 15. 15.
grid-f
0. 0.
grid-r
0. 0.
grid-kf grid-kr L-Boil NH
1. 1
*
*
Containment SS stuctures (Thinner ones)
*
#-HS #-MP geotype SS-ini L-coord. reflood
10703000 1 5 1
0 7.5
*
mesh-loc format-flag
10703100 0
1
*
#-Intvl R-coord. (radial info.)
10703101 4
7.525
*
comp-# interval-# (radial info.)
145
bvol-ind axial#
10703201 4
4
source value interval-# (radial info.)
*
4
10703301 0.0
*
initial temperature flag (if flag=0 or -1)
10703400 -1
temp-i
temp-2 temp-3
*
10703401 303.15 303.15 303.15 303.15 303.15
increment BC option surf.code height NH
* L-B B.Vol.#
0
700. 1
160
070010000
10000
10703501
increment BC option surf.code height NH
* R-B B.Vol.#
0
700.0 1 * Insulate
0
0
10703601 0
* Source source-type multiplier DHeat-Left DHeat-Right NH
0.
0.
1
10703701 0
0.
*
9-words format option
10703800 1 *This 12-words format
* Add L-B Dh HL-f HL-r grid-f grid-r grid-kf grid-kr L-Boil NH
15. 0. 0. 0. 0. 1. 0. 1.1 1.0 1
10703801 42.79 15.
*
* Add R-B Dh HL-f HL-r
15.
10703901 42.79 15.
grid-r
0. 0.
grid-f
0. 0.
grid-kf grid-kr L-Boil NH
1. 1
*
*
*+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
+
*---------------------------------------------------------
*
heat
proper
s t ructures
t i e s
*
*--------------------------------------------------------*
20100100
20100200
20100300
20100400
20100500
20100600
20100700
20100800
20100900
20101000
tbl/fctn
tbl/fctn
tbl/fctn
s-steel
tbl/fctn
tbl/fctn
tbl/fctn
tbl/fctn
tbl/fctn
tbl/fctn
1
3
1
tbl/fctn
tbl/fctn
tbl/fctn
tbl/fctn
tbl/fctn
1
1
1
1
1
1
1
1
3
1
1
* UO-2
* gap for average rods
* zircaloy
* s. steel (default)
1 * inconel
1 * ferrit SS
1 * austenit SS
1 * gap for hot rod
1 * inconel for energy balance
1 * heater (MgO)
1
1
1
*
20101100
20101200
20101300
20101400
20101700
1
1
1
1
1
*
*
*
*
*
U-TRU-Zr (90:10 weight fraction)
UC-SiC (50:50 volume fraction)
SiC for the Lower-Upper Reflector
Concrete
Insulator
*-----------------------------------------------------------------
fuel UC
*
temp[k] lamda[w/m-k]
lamda[w/m-k]
temp[k]
*
373.15 21.4321
20100101 273.15 21.7
20100102 473.15 21.2364 573.15 21.1129
20100103 673.14 21.0616 773.15 21.0825
20100104 873.15 21.1756 973.15 21.3409
20100105 1073.15 21.384 1173.15 21.532
1373.15 21.828
20100106 1273.15 21.68
20100107 1473.15 21.976 1573.15 22.124
20100108 1673.15 22.272 1773.15 22.42
20100109 1873.15 22.568 1973.15 22.716
20100110 2073.15 22.864 2173.15 23.012
146
20100111
20100112
20100113
20100114
20100115
20100116
23.16
23.456
23.752
24.048
24.344
25.084
2273.15
2473.15
2673.15
2873.15
3073.15
3573.15
2373.15
2573.15
2773.15
2973.15
3173.15
4873.15
23.308 *Extrapolated
23.604 *Extrapolated
23.9 *Extrapolated
24.196 *Extrapolated
24.492 *Extrapolated
27.008 *Extrapolated
temp[k]
lamda[w/m-k]
*---------------------------------------------------------------
*
gap gas average rods
*
gas type mole fraction
20100201 helium 0.9511
20100202 argon 0.0396
20100203 nitrogen 0.0008
20100204 xenon 0.0076
20100205 krypton 0.0008
*------------------------------------------------------------
*
*
huellrohr zircaloy
temp[k]
lamda[w/m-k]
*
20100301
20100302
20100303
20100304
20100305
20100306
20100307
20100308
20100309
20100309
273.15
473.15
673.15
873.15
1073.15
1273.15
1473.15
1673.15
1873.15
1873.15
13.6
14.8
16.9
19.5
22.8
26.8
31.7
37.3
43.5
43.5
373.15 14.1
573.15 15.8
773.15 18.1
973.15 21.1
1173.15 24.6
1373.15 29.2
1573.15 34.4
1773.15 40.4
1973.15 46.6
4973.15 46.6
* test
*-----------------------------------------------------------------
*
inconel
*
temp(k) lamda(w/m3-k) temp(k) lamda(w/m3-k)
20100501 294.3 14.9
366.0
15.7
20100502 477.0 17.5
588.7
19.2
20100503 699.8 20.9
810.9
22.8
20100504 1500.0 22.8
*-----------------------------------------------------------------
*
ferrit
*
temp[k]
lamda[w/m-k] temp[k] lamdal[w/m-k]
20100601 73.15
44.
373.15 44. *arbitrarily extended
20100602 473.15
43.
573.15 42.
20100603 673.15
40.
773.15 39.
20100604 873.15
39.
973.15 39.
20100605 1073.15 39.
1173.15 39.
20100605 1073.15 39.
1973.15 39. *arbitrarily extended
20100606 5000.0
39.
*-----------------------------------------------------------------
*
austenit
*
temp[k] lamda[w/m-k]
temp[k]
lamda[w/m-k]
20100701 293.15 14.24 413.15 16.7
20100702 523.15 18.6 683.15 18.6
20100703 773.15 20.9 873.15 20.9
20100704 973.15 20.9 2000.
20.9
20100704 973.15 20.9 4000.
20.9 *!test
*-----------------------------------------------------------------
*
gap
gas
hot rod
*
gas type mole fraction
20100801 helium 0.9079
147
20100802
20100803
20100804
20100805
argon 0.0378
nitrogen 0.0049
xenon 0.0445
krypton 0.0050
*-----------------------------------------------------------------
*
Inconel Property Tuning for Energy Balance Factor : 1.55
*
20100901
20100902
20100903
20100904
294.3 23.09
477.0 27.13
699.8 32.39
1500.0 35.34
366.0
588.7
810.9
24.34
29.76
35.34
*
*----------------------------------------------------------------
* PZR Heater - MgO (010)
temp (k) thermal conductivity (w/m.k)
*
20101001 .29320e+03 .81400e+02
20101002
.12732e+04 .10047e+03
.22532e+04 .11954e+03
20101003
*-----------------------------------------------------------------
* U-TRU-Zr (90:10 weight fraction)
*
temp (k) thermal conductivity (w/m.k)
20101101 373. 21.16 600. 23.1546
20101102 900. 25.0209 938. 25.2094
20101103 938.01 25.2095 1049. 25.707
20101104 1049.01 25.0707 1132.3 26.0308
*--------------------------------------------------------------
* UC-SiC (50:50 volume fraction)
*
temp (k) thermal conductivity (w/m.k)
20101201 373. 20.9195 600. 20.7434
20101202 900. 20.7767 1200. 20.4998
20101203 1500. 20.3775 1800. 20.2394
20101204 2100. 20.0847 2400. 19.9125
*
*-------------------------------------------------------------
*
SiC
*
temp(k) lamda(w/m.k) temp(k)
15.
2400. 15.
20101301 273.
lamda(w/m.k)
*-----------------------------------------------------------
* Concrete
20101401 1.4
* Insulator
20101701 0.34
*--------------------------------------------------------*
volumetric heat capacity
*--------------------------------------------------------*
fuel UC
temp[k]
cp[j/m3-k]
*
temp[k]
20100151
20100152
20100153
20100154
20100155
20100156
20100157
20100158
20100159
273.150 3.536e6
3.536e6
500.
700.
3.536e6
3.536e6
900.
1100. 3.536e6
1300. 3.536e6
1500. 3.536e6
1700. 3.536e6
1900. 3.536e6
400.
600.
800.
1000.
1200.
1400.
1600.
1800.
2000.
*
cp[j/m3-k]
3.536e6 *average
3.536e6
3.536e6
3.536e6
3.536e6
3.536e6
3.536e6
3.536e6
3.536e6
148
20100160
20100161
20100162
20100163
2100.
2300.
2500.
3000.
3.536e6
3.536e6
3.536e6
3.536e6
2200.
2400.
2600.
5000.
3.536e6
3.536e6
3.536e6
3.536e6
*----------------------------------------------------------------
*
gap
gas
*
temp[k]
cp[j/m3-k] temp[k]
3273.15
20100251 273.15 5.4
cp[j/m3-k]
5.4
*-----------------------------------------------------------------
*
huellrohr zicaloy
*
temp[k] cp[j/m3-k] temp[k] cp[j/m3-k]
573.15 2.079e6
20100351 273.15 1.881e6
20100352 773.15 2.211e6
903.15 2.290e6
1083.15 2.376e6
20100353 923.15 2.376e6
20100354 1103.15 3.630e6
1123.15 4.455e6
20100355 1143.15 4.950e6
1163.15 5.115e6
1203.15 4.455e6
20100356 1183.15 4.950e6
20100357 1213.15 3.360e6
1243.15 2.376e6
20100358 2073.15 2.376e6
20100358 4073.15 2.376e6 *test
*-----------------------------------------------------------------
*
inconel
*
temp(k) cp(j/m3-k)
20100551 273. 3.988e6
20100552 373. 4.169e6
20100553 573. 4.703e6
20100554 773. 5.593e6
20100555 973.
7.482e6
20100556 2000. 7.482e6
temp(k)
293.0
473.0
673.0
873.0
1000.0
4000.
cp(j/m3-k)
3.916e6
4.418e6
5.095e6
6.307e6
7.482e6
7.482e6 *Arbitrary Extended
*-----------------------------------------------------------------
*
ferrit
*
templ[k]
cp[j/m3-k]
temp[k] cp[j/mf-k]
20100651 93.15 3.611e6 373.15 3.847e6 *Arbitrary extended
20100652 473.15 4.082e6 573.15 4.396e6
20100653 673.15 4.788e6 773.15 5.338e6
20100654 2000. 5.338e6 4000.00 5.338e6 *Arbitrary Extended
*-----------------------------------------------------------------
*
austenit
*
temp[k] cp[j/m3-k]
temp[k] cp[j/m3-k]
20100751 293.15 3.572e6 368. 3.837e6
20100752 478.15 4.102e6 588.15 4.333e6
20100753 698.15 4.465e6 813.15 4.597e6
20100754 873.15 4.465e6 2000. 4.465e6
20100754 873.15 4.465e6 4000. 4.465e6 *test
*-----------------------------------------------------------------
*
gap
gas
*
temp[k] cp[j/m3-k] temp[k]
cp[j/m3-k]
20100851 273.15 5.4
3273.15 5.4
*------------------------------------------------------------------
*
*
Inconel
temp(k)
cp(j/m3-k)
temp(k)
cp(j/m3-k)
*
20100951 273. 3.988e6
294.3
3.740e6
20100952 366.5 3.917e6
477.6
4.094e6
20100953 588.8 4.270e6
699.9
4.446e6
20100954 811.0 4.658e6
2000.0
4.658e6
20100955 4000. 4.65836 *Arbitrary Extended
149
*-----------------------------
------------------
---------
-----
* PZR Heater - MgO (010)
*
temp (k) volumetric heat capacity (j/m3.k)
.293e+03 .2581e+07
20101051
.450e+03 .2835e+07
20101052
.3402e+07
20101053 .800e+03
.112e+04 .3726e+07
20101054
.144e+04 .4050e+07
20101055
*-------------------------------------------------------------
* U-TRU-Zr (90:10 weight fraction)
temp (k) volumetric heat capacity (j/m3.k)
*
20101151 373. 2.21306e6 600. 2.58049e6
20101152 900. 3.25756e6 938. 3.35867e6
20101153 938.01 3.03142e6 1049. 2.98995e6
20101154 1049.01 2.71774e6 1132.3 3.05993e6
*-------------------------------------------------------
* UC-SiC (50:50 volume fraction)
temp (k) volumetric heat capacity (j/m3.k)
*
20101251 373. 2.58160e6 600. 2.74160e6
20101252 900. 3.22160e6 1200. 3.70160e6
20101253 1500. 3.86160e6 1800. 3.95760e6
20101254 2100. 4.02160e6 2400. 4.10160e6
*--------------------------------------------------
* SiC
temp(K) Cp(J/kg-K) temp(K) Cp(J/kg-K)
*
600. 600.
500.
20101351 273.
20101352 900. 900. 1200. 1200.
20101353 1500. 1300. 1800. 1360.
20101354 2100. 1400. 2400. 1450.
--------
*-----------------------------------------------
* Concrete
20101451 840.
* Insulator
20101751 1050.
*---------------------------------------------------
*
power
table
*---------------------------------------------------
*20210000
*20210001
*20210002
*20210003
*20210004
*20210005
*20210006
*20210007
*20210008
*20210009
*20210010
*20210011
*20210012
*20210013
*20210014
*20210015
*20210016
*20210017
*20210018
*20210019
power 503 1.
1.0
-1.
0.20267
0.
0.12720
5.
0.11631
10.
0.08037
20.
0.06289
30.
0.05148
40.
0.04565
50.
0.04097
70.
0.03726
100.
0.03448
150.
0.03268
200.
0.03024
300.
0.02862
400.
0.02741
500.
0.02683
600.
0.02486
800.
1000. 0.02362
1300. 0.02211
2775.0e6
150
*20210020
*20210021
*20210022
*20210023
*20210024
*20210025
*20210026
*20210027
*20210028
1600.
2000.
2500.
3000.
3500.
4000.
4500.
5000.
6000.
0.02090
0.01960
0.01836
0.01736
0.01657
0.01590
0.01537
0.01490
0.01404
*---------------------------------------------------------
*
control variables
*--------------------------------------------------------*
* Temperature Drop core
20510100 DeltT sum 1.0 360. 1
20510101 0.0 -1.0 tempg
100050000
20510102
1.0 tempg
300010000
*
* Estimated extracted Q (Core)
20510200 EstimQ mult 5192.4 6.0e8
20510201 cntrlvar
101
20510202 mflowj
100040000
1
*
* MAX Temperature Cladding: Control variable 103
20510300 max-clad stdfnctn 1.0 1310.995 1
20510301 max httemp 251100107 httemp 251100108
20510302
httemp 251100207 httemp 251100208
20510303
httemp 251100307 httemp 251100308
20510304
httemp 251100407 httemp 251100408
20510305
httemp 251100507 httemp 251100508
20510306
httemp 251100607 httemp 251100608
20510307
httemp 251100707 httemp 251100708
20510308
httemp 251100807 httemp 251100808
** reynolds number (De = 0.0127)
20510800 re-no0 mult 0.0127 2.783415 1
20510801 rhog 250040000 velg 250040000
20510900 re-no div 1.0 67608.9 1
20510901 viscg 250040000 cntrlvar 108
*
* MAX Temperature Fuel: Control variable 110
20511000 max-fuel stdfnctn 1.0 1310.995 1
20511001 max httemp 251100401 httemp 251100402
20511002
httemp 251100403 httemp 251100404
20511003
httemp 251100501 httemp 251100502
20511004
httemp 251100503 httemp 251100504
20511005
httemp 251100601 httemp 251100602
20511006
httemp 251100603 httemp 251100604
20511007
httemp 251100701 httemp 251100702
20511008
httemp 251100703 httemp 251100704
20511009
httemp 251100801 httemp 251100802
20511010
httemp 251100803 httemp 251100804
*
* Energy Balance in core 250 and 251
20511100 Core-E sum 1.0 6.+8 1
20511101 0.0 1.0 q
250010000
20511102
1.0 q
250020000
20511103
1.0 q
250030000
151
20511104
20511105
20511106
20511107
20511108
20511109
20511110
20511111
20511112
20511113
20511114
20511115
20511116
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
q
q
q
q
q
q
q
q
q
q
q
q
q
250040000
250050000
250060000
250070000
250080000
251010000
251020000
251030000
251040000
251050000
251060000
251070000
251080000
**
* Heat loss from the primary wall heat structures
* Hydrodynamic components 100, 210, 211, 290, 291, 610, 611, 666, 676,
670
* DHR HX 1 (650): Control varialbe 120
20512000 DhrHX1HS sum 1.0 .1704288 1
20512001 0.0 1.0 q
650010000
1.0 q
650020000
20512002
20512003
1.0 q
650030000
20512004
1.0 q
650040000
20512005
1.0 q
650050000
*Power generated in the core Control variable 123
20512300 corepowg
sum 1.0 600.0e6 1
0.0 1.0 htpowg 2501001
20512301
20512302
1.0 htpowg 2501002 1.0 htpowg 2501003
1.0 htpowg 2501004 1.0 htpowg 2501005
20512303
20512304
1.0 htpowg 2501006 1.0 htpowg 2501007
20512305
1.0 htpowg 2501008 1.0 htpowg 2511001
20512306
1.0 htpowg 2511002 1.0 htpowg 2511003
20512307
1.0 htpowg 2511004 1.0 htpowg 2511005
20512308
1.0 htpowg 2511006 1.0 htpowg 2511007
20512309
1.0 htpowg 2511008
* DHR HX 2 (651): Control varialbe 125
.1704288 1
20512500 DhrHX2HS sum 1.0
651010000
20512501 0.0 1.0 q
20512502
1.0 q
651020000
20512503
1.0 q
651030000
20512504
1.0 q
651040000
20512505
1.0 q
651050000
* DHR HX 1 (710): Control varialbe 126
20512600 DhrHX1CS sum 1.0
.665619 1
20512601 0.0 1.0 q
710010000
1.0 q
710020000
20512602
710030000
20512603
1.0 q
1.0 q
710040000
20512604
20512605
1.0 q
710050000
* DHR HX 2 (711): Control varialbe 127
20512700 DhrHX2CS sum 1.0 .665619 1 *8.60957-6
20512701 0.0 1.0 q
711010000
20512702
1.0 q
711020000
152
20512703
1.0 q
711030000
20512704
1.0 q
711040000
20512705
q
1.0
711050000
* H201 (750)
Control varialbe 128
20512800 H201 sum 1.0 8.10906-6
20512801 0.0
1.0 q
750010000
20512802
1.0 q
750020000 1.0
20512803
1.0 q
750040000 1.0
20512804
1.0 q
750060000 1.0
20512805
1.0 q
750080000 1.0
20512806
1.0 q
750100000 1.0
20512807
1.0 q
750120000 1.0
20512808
1.0 q
750140000 1.0
20512809
1.0 q
750160000 1.0
20512810
1.0 q
750180000 1.0
20512811
1.0 q
750200000
* H202 (751): Control varialbe 129
20512900 H202 sum 1.0 3977.325
20512901 0.0
1.0 q
751010000
20512902
751020000 1.0
1.0 q
20512903
751040000 1.0
1. 0 q
20512904
1.0 q
751060000 1.0
20512905
1.0 q
751080000 1.0
20512906
1.0 q
751100000 1.0
20512907
1.0 q
751120000 1.0
20512908
1.0 q
751140000 1.0
20512909
1.0 q
751160000 1.0
20512910
1. 0 q
751180000 1.0
20512911
1.0 q
751200000
20513000
20513001
Firder
tempg
20513100
20513101
Secder diffrend
cntrlvar 130
diffrend 1.0
251080000
1.0
750030000
750050000
750070000
750090000
750110000
750130000
750150000
750170000
750190000
751030000
751050000
751070000
751090000
751110000
751130000
751150000
751170000
751190000
0. 1
0.
1
*ctlvar name type factor init f c min
20560000 shaftl shaft 1.0 376.991 1
1
max
0.1
*ctlvar cv iner fric type
comp type comp
20560001 990 729.867 0.0 turbine 510
20560002
cprssr 550
20560003
cprssr 580
20560004
generatr 600
*
iner fric trip discon
20560006 376.991 376.991 1270.95 0.0 360 0
* added shaft torque from a control variable representing a resistor
bank
20599000
20599001
shftTrql
time 0 990
function
1.0
1.0
1
* Table giving resistor bank torque versus time for Ix shaft
153
20299000
*
20299001
20299002
reac-t
time
0.0
3.5
529
torque
0.
-100000.
-*-
$:
* compute generator torque (N-m) and power (mw)
$
*ctlvar name type factor
20560200 gentrql sum 1.0
init f c min
407472.4 1
max
*
*ctlvar a0 al v1
pl
a2 v2
p2
20560201 0.0 1.0 turtrq 510
1.0 cprtrq
20560202
1.0 cprtrq 580
*ctlvar name type factor init f c min
153613424. 1
20560400 genpowl mult 1.0
550
max
*
*ctlvar v1
pl
v2
20560401 cntrlvar 600
p2
cntrlvar
602
$
* compute turbine shaft power in MW
$
*ctlvar name type factor init f c min max
20562000 turpowl sum 1.e-6 411.063 1 1 l.e-6
*
*ctlvar a0 al v1
pl
20562001 0.0 1.0 turpow
a2 v2
510
*
$=
*control variables to calculate total power transfered in recouperator
*
20503000
20503001
20503002
520070000
20503003
520110000
20503004
520150000
20503005
520190000
20503006
520230000
20503007
520270000
20503008
rchQl sum 1.0 -6.00586+8 1
1.0 q 520010000 1.0 q 520020000 1.0 q 520030000
0.0
1.0 q 520040000 1.0 q 520050000 1.0 q 520060000 1.0 q
1.0 q
520080000
1.0 q
520090000
1.0 q
520100000
1.0 q
1.0 q
520120000
1.0 q
520130000
1.0 q
520140000
1.0 q
1.0 q
520160000
1.0 q
520170000
1.0 q
520180000
1.0 q
1.0 q
520200000
1.0 q
520210000
1.0 q
520220000
1.0 q
1.0 q
520240000
1.0 q
520250000
1.0 q
520260000
1.0 q
1.0 q
520280000
1.0 q
520290000
1.0 q
520300000
20503100
205031001 rccQl sum 1.0 6.00586+8 1
1.0 q 590010000 1.0 q 590020000 1.0 q 590030000
205031012 0.0
2050310270000 1.0 q 590040000 1.0 q 590050000 1.0 q 590060000 1.0 q
590070000
154
20503103
590110000
20503104
590150000
20503105
590190000
20503106
590230000
20503107
590270000
20503108
1.0
590080000
1.0
590090000
1.0
590100000
1.0
1.0
590120000
1.0
590130000
1.0
590140000
1.0
1.0
590160000
1.0
590170000
1.0
590180000
1.0
1.0
590200000
1.0
590210000
1.0
590220000
1.0
1.0
590240000
1.0
590250000
1.0
590260000
1.0
1.0
590280000
1.0
590290000
1.0
590300000
*control variables to calculate total power transfered in precooler
20503200
20503201
20503202
530070000
20503203
530110000
20503204
530150000
20503205
530190000
20503206
20503300
205033001
205033012
20503302
133070000
20503303
133110000
20503304
133150000
20503305
133190000
20503306
pc_hQl sum 1.0 -152171632.
0.0
1.0 q 530010000 1.0 q 530020000 1.0 q 530030000
1.0 q 530040000 1.0 q 530050000 1.0 q 530060000 1.0 q
1.0 q
530080000
1.0 q
530090000
1.0 q
530100000
1.0 q
1.0 q
530120000
1.0 q
530130000
1.0 q
530140000
1.0 q
1.0 q
530160000
1.0 q
530170000
1.0 q
530180000
1.0 q
1.0 q
530200000
pc_cQl sum 1.0 152171632. 1
1.0 q 133010000 1.0 q 133020000 1.0 q 133030000
0.0
1.0 q 133040000 1.0 q 133050000 1.0 q 133060000 1.0 q
1.0 q
133080000
1.0 q
133090000
1.0 q
133100000
1.0 q
1.0 q
133120000
1.0 q
133130000
1.0 q
133140000
1.0 q
1.0 q
133160000
1.0 q
133170000
1.0 q
133180000
1.0 q
1.0 q
133200000
*
*control variables to calculate total power transfered in inter-cooler
*
20503400
20503401
20503402
570070000
20503403
570110000
20503404
570150000
20503405
570190000
20503406
20503500
20503500
ic hQl sum 1.0 -128865440. 1
0.0
1.0 q 570010000 1.0 q 570020000 1.0 q 570030000
1.0 q 570040000 1.0 q 570050000 1.0 q 570060000 1.0 q
1.0 q
570080000
1.0 q
570090000
1.0 q
570100000
1.0 q
1.0 q
570120000
1.0 q
570130000
1.0 q
570140000
1.0 q
1.0 q
570160000
1.0 q
570170000
1.0 q
570180000
1.0 q
1.0 q 570200000
iccQl sum 1.0
ic~cQl sum 1.0
128865440. 1
128865440. 1
155
20503501
20503502
143070000
20503503
143110000
20503504
143150000
20503505
143190000
20503506
0.0
1.0 q
1.0 q 143010000 1.0 q 143020000 1.0 q 143030000
143040000 1.0 q 143050000 1.0 q 143060000 1.0 q
1.0 q
143080000
1.0 q
143090000
1.0 q
143100000
1.0 q
1.0 q
143120000
1.0 q
143130000
1.0 q
143140000
1.0 q
1.0 q
143160000
1.0 q
143170000
1.0 q
143180000
1.0 q
1.0 q
143200000
$
*control variables to calculate total power to compressor
*
*ctlvar name type factor
20503600 qrcl_1 mult -1.0
init f c min
130462160. 1
max
*
*ctlvar vI
pl
20503601 cprtrq
v2
550
p2
cprvel
550
*
*ctlvar name type factor init f c min
126931640. 1
20503700 qrch_1 mult -1.0
max
*
*ctlvar v1
pl
20503701 cprtrq
v2
580
p2
cprvel
580
*
20503800
20503801
cprl sum 1.0 2.57394+8 1
0.0 1.0 cntrlvar 036 1.0 cntrlvar 037
*
20503900
20503901
cprlpf sum 1.0 2.4e6 1
0.0 1.0 p 550010000
-1.0
cprhead 550
*
20504000
20504001
Rpl div 1.0 1.8 1
cntrlvar 039 p 550010000
*
20504100
20504101
cpr2pf sum 1.0 4.5e6 1
0.0 1.0 p 580010000
-1.0
*
20504200
20504201
Rp2 div 1.0 1.56 1
cntrlvar 039 p 580010000
156
cprhead 580
APPENDIX C: TABLE OF PROPA GA TED UNCERTAITY
11.3.
HeatTranfer
Heat Transfer
Roughness
In the core
Valve 674
Leakage
Valve 665
Leakage
Heat Transfer
Coefficinentin
Containment
1
7.0266E-05
0.660972906
0.132791381
1.018099269
0.175240146
756.4283936
2
3.17861E-05
0.464606103
0.009216567
0.619031756
1.49147449
908.4799804
3
1.41968E-05
0.189936412
0.446353642
0.518304501
4.089563936
805.6640345
4
0.000165969
0.2247406
1.665210385
3.074084819
1.339039701
774.7889025
5
2.23325E-05
0.110839306
0.363779265
3.883312254
0.543303791
679.3242198
6
8.95976E-05
0.082665107
0.273528511
0.094501105
0.936337946
546.7819977
7
2.53847E-05
0.392584938
0.085119427
1.183833099
0.646817192
653.69233
8
4.4716E-05
0.032207799
0.215695098
1.643178094
0.376749072
723.5864463
9
5.38544E-05
0.607582295
0.156639456
1.772914465
1.793946565
597.3626375
10
7.85191E-05
0.302996778
0.042048843
0.277030229
2.391928364
732.6888426
11
3.85214E-05
0.17446045
0.09064391
4.829592916
0.293658031
703.6532569
12
8.47645E-06
0.140217132
0.220896755
0.42291142
0.864267335
759.3058686
13
5.91768E-05
0.058180793
0.70785134
0.838450117
0.465954267
696.1311388
14
2.84935E-05
0.012386872
0.534292341
2.266994934
1.104884296
823.2713509
15
1.82596E-05
0.337699928
0.348002328
0.745117621
0.761977965
846.9083615
16
0.000123131
0.890796357
0.023758162
1.333115501
0.429398495
633.8352274
17
7.08761E-06
0.066021338
0.127291225
11.24755112
1.596157589
841.0356824
18
1.10777E-05
0.099241677
0.061949683
1.369543295
1.013147351
770.1586118
19
0.000105528
0.529594859
0.189806486
0.948642402
0.727023454
749.8937713
157
Coefficient insfer Shaft Moment
Coecntin
of Inertia
Core
20
4.31121E-05
0.74219072
0.114714985
3.263201796
1.224111492
890.9974519
21
0.000211663
0.03001568
0.069037775
0.210871326
0.676329216
739.7666992
22
1.92448E-05
0.202227439
0.985357812
0.905538264
1.170526951
644.3272329
23
3.40267E-05
0.263548363
0.178068757
0.803267482
3.684155094
626.2864629
24
4.96232E-05
0.498487678
0.238331675
0.468322129
0.095135605
720.8448245
25
0.00014868
0.043266545
0.286472444
2.184673244
0.802686297
807.6559167
26
1.71049E-05
1.190170101
0.512037361
1.487914895
0.242057146
693.869699
27
5.68576E-05
0.001891644
0.593915737
1.121569675
0.409672324
663.102377
28
2.34316E-05
0.422684746
0.321484425
0.347961093
2.105991987
795.8641541
29
3.63424E-05
0.127905542
0.852944013
0.689984288
0.511600116
712.7091911
30
6.49453E-05
0.256755913
0.422403824
2.608512339
0.328936234
684.2025295
31
8.00589E-05
0.158081862
0.017396258
1.921065859
0.574820132
782.6452305
32
2.91641E-05
0.330425174
0.039769783
0.542943227
1.919305918
589.7391975
33
4.68492E-05
0.641145484
0.678139931
0.770016585
0.25968491
812.7976894
34
9.93625E-05
0.80248295
0.911992663
1.061765697
2.910536583
675.4663903
35
8.51434E-05
0.154193833
0.30223248
1.397918526
0.889602906
659.5673134
36
5.12343E-05
0.084045934
0.333844337
0.303841247
0.792966876
825.8242815
37
7.10865E-05
0.480768573
1.230679167
1.908661706
1.247906264
735.2691428
38
0.000111937
0.23343891
0.163818188
0.811362806
0.152467084
766.0256004
39
2.0305E-05
0.136108256
0.490839118
1.721271504
0.397270165
691.1926356
40
9.97261E-06
0.994760314
0.561209485
2.350701033
0.999122583
680.3988408
41
2.17877E-05
0.187909689
0.24745941
3.571845903
0.4874615
698.6515597
158
42
1.48581E-05
0.244850439
0.183940052
1.239715178
1.684962153
834.5824853
43
4.71902E-05
0.282812486
0.202202188
0.358308616
2.057624559
744.2958614
44
3.09792E-05
0.403472191
0.793651269
6.032402101
0.698321791
753.7330773
45
7.38153E-05
0.060647096
0.629844302
0.71082589
0.956883392
727.6012104
46
0.00020055
0.071397709
0.082152443
2.507926869
1.142414957
919.8463003
47
2.77006E-05
0.104256214
0.153300021
5.406115063
8.141160654
717.6353089
48
3.98161E-05
0.700051648
0.001308486
0.884653856
1.560774312
568.5798634
49
4.62055E-06
0.315619703
0.383399114
1.591284501
0.631478997
649.990263
50
1.61458E-05
0.00693723
0.46147984
1.291044363
2.286157212
620.3083227
51
6.56956E-05
0.17005815
0.231037463
1.54223527
1.041974271
614.5442327
52
6.14829E-05
0.018504666
0.012842897
4.001604887
0.361890083
787.9536835
53
2.61785E-05
0.022433357
0.316280157
0.660842505
0.344565861
764.3418628
54
0.000267854
1.442496364
0.054688522
0.394960618
0.276108579
506.9498172
55
1.24528E-05
0.361764165
0.118231636
0.250464186
0.831776376
709.2587003
56
0.000133637
0.117707471
0.100020368
0.575748717
0.455933376
798.5982391
57
2.46989E-05
0.094621349
0.03588993
2.021533534
1.386404602
640.4817296
58
5.5652E-05
0.049276257
0.258345944
0.605107028
0.212640618
670.8181273
59
1.74366E-05
0.449463712
0.142381726
1.115250099
0.524400738
792.6038844
60
3.79521E-05
0.038705296
0.075183345
0.181204116
0.560520061
740.1853296
61
9.74176E-05
0.272326653
0.106640922
0.484303178
2.635348042
857.0121359
62
4.16683E-05
0.210614439
0.051236791
0.997587303
0.70547236
870.6038543
63
3.56232E-05
0.574585443
0.406903451
2.757981398
0.608032193
776.9877291
159
64
3.30958E-05
0.374395138
0.028567636
0.443542793
1.406811368
714.4770836
65
2.44393E-05
0.03892315
0.037643374
1.826227042
0.743613759
790.4907116
66
3.26663E-05
0.429736516
0.073220858
2.374057349
0.66304439
762.5381162
67
0.000119456
0.853064915
0.110295296
2.700746814
0.350313969
697.3852592
68
4.24467E-05
0.163285009
0.057242128
0.163381672
0.44344617
667.9643603
69
6.11709E-05
0.182661765
0.194803481
0.323280366
0.289654677
819.3971924
70
1.44549E-05
0.177547568
0.031614643
1.255017446
0.4822816
754.0690469
71
3.96156E-05
0.294931273
0.663103609
0.515879692
0.118911905
810.9794981
72
1.63018E-05
0.292796158
0.396770153
4.520676725
0.756463197
605.3773675
73
9.44872E-05
0.05127336
0.294894594
1.217860942
3.045780555
881.102285
74
1.35938E-05
0.562509747
0.095951235
1.060178579
2.559356379
786.2160539
75
1.56751E-05
0.069275548
0.327920832
2.203124185
0.336998293
750.443934
76
9.2457E-05
0.220260843
0.264218317
0.386888355
0.92479469
771.8319671
77
3.50952E-05
0.321362252
1.155321411
0.787872797
1.950232297
773.9635894
78
5.46275E-05
0.089781232
0.160602313
1.744233057
0.903230525
667.0187805
79
4.80789E-05
0.21184961
0.357060873
1.430553609
0.62257917
726.377878
80
1.19785E-05
0.348104379
0.060423816
1.51025574
1.281580227
901.8600227
81
2.29841E-05
0.078958706
0.066758276
0.921965926
0.549252891
689.3581492
82
5.76447E-05
0.109910569
0.207762362
0.234382257
0.418804468
542.6183457
83
4.8909E-05
0.312370023
0.477193119
2.429644306
0.588941377
779.4032731
84
4.05737E-05
0.387344337
0.828494585
1.564471368
1.629139496
566.0462942
85
9.09296E-06
0.015774464
0.138237619
1.312702309
1.306318855
780.6770487
160
86
7.22034E-05
0.491041341
0.006652834
1.360475912
0.870487068
646.5550358
87
7.62102E-05
0.405617924
0.018203018
1.464275245
0.217787688
631.2502285
88
8.1427E-06
0.198004657
0.341567074
0.218745727
1.350890534
829.7959148
89
6.33097E-05
1.066584672
0.393328526
3.731597047
1.756550384
736.7537934
90
1.07823E-05
0.063723513
1.027471598
1.087912879
0.600179238
618.2618736
91
3.42523E-05
0.026950605
0.281080473
2.933790801
1.542390549
661.3841643
92
3.00196E-05
0.238012053
0.143020405
0.639826242
1.131315686
723.0224825
93
0.000129871
0.124871384
1.416088806
0.328154832
0.252036602
607.7127042
94
0.000154807
1.640795395
0.174494136
0.698446807
1.458026427
687.2560797
95
5.83034E-05
0.114459764
0.548945478
4.244041273
0.30499423
691.5167995
96
2.08798E-05
0.054269715
0.049615326
0.969358208
0.158179792
745.988633
97
4.6118E-05
0.046090401
0.72803977
0.431048625
0.228051476
719.5882072
98
3.19744E-05
0.123509661
0.378526192
5.066997272
1.194993691
730.2204229
99
0.000109476
0.091293959
0.202069973
0.28116126
2.718226393
828.5424988
100
0.000101622
0.162009876
0.021353242
1.178274754
2.191621088
866.6712278
101
0.000117389
0.197024004
0.089317371
0.632726739
1.862677253
682.3440286
102
1.81686E-05
1.116133243
0.631878624
0.50362288
0.476034599
706.2820555
103
0.000140123
0.3694106
0.123210426
2.116812651
3.350699786
676.6710866
104
2.35482E-05
0.231032974
0.045327924
3.093001052
0.437834921
700.4461747
105
0.000184661
0.00341441
0.011420538
1.036389138
0.951400214
800.1570805
106
0.000350929
0.007558315
0.752383237
2.849447745
1.031748519
840.016604
107
3.66486E-05
0.034792339
0.148018768
1.838354829
1.068334272
704.8611658
161
108
5.27417E-05
0.267794393
0.166937809
0.722632293
2.239221847
742.5520429
109
2.72498E-05
0.438173699
0.310950321
1.687224992
0.528280225
652.8748077
110
8.64598E-05
0.689489885
0.078987467
0.414106752
0.846720021
638.5343373
111
5.76494E-06
0.720264048
0.567437747
0.954076081
0.388809242
710.7008624
112
2.59569E-05
0.45873879
0.500676834
2.066317956
0.777648147
578.8421024
113
2.89684E-05
0.076801692
0.288628703
3.448935736
0.49654075
803.3525057
114
1.87046E-05
0.014315049
0.432706689
7.888527292
0.653884589
767.0671491
115
2.68496E-05
0.589125745
0.003257401
0.567182096
0.689344201
758.0042827
116
5.1259E-05
0.144203165
0.610120945
0.756656021
0.972753315
862.1368141
117
8.27308E-05
0.622005761
0.252690176
0.893303892
4.6458655
793.8374791
118
3.06792E-05
0.544848006
0.105402894
0.371657756
0.823148669
595.2374457
119
0.000242648
0.100470863
0.232242065
0.463772479
0.372780363
952.8508248
120
2.12095E-05
0.771453316
0.245206874
0.555995609
0.312550768
729.8084907
121
3.77208E-05
0.147013488
0.890147715
0.135454779
1.435246354
627.4004514
122
6.81034E-05
0.248773951
0.027479927
0.86335716
1.078165163
672.4727793
123
4.45943E-05
0.511529166
0.466634545
1.983037627
5.38763593
851.0149522
124
1.27816E-05
0.951530839
0.098224977
0.831457732
1.197266703
747.4191242
125
7.78064E-05
0.132872215
0.221597428
0.675599703
0.566604491
733.6726776
126
6.6777E-05
0.022776219
0.188431304
7.610320216
0.717407639
714.6749388
127
1.97961E-05
0.34663953
0.433029247
1.158006383
1.743479501
816.8852588
128
4.36691E-05
0.276821361
0.131480541
0.594252985
0.197257333
656.443749
162
11.4.
APPENDIX D: UTILIZED ALGORITHMS
All algorithms that are present here are for MATLAB® 7.0. They have not been
tested on previous versions of the software. They are presented as a series of steps
required to finally get the number of failures for each evaluated failures mode. The first
algorithm that is presented was used to create the sample offered in Appendix C.
function x = LHS(n,v,N,iter)
t
J
=
1;
for j=1:iter
c1c;
J
X = getsample(n,v,:'..,zeros (1,v));
for i=1:N
Y = ceil((n*2^i)*X);
Z = getsample(n*2:.iv,
",Y)
X = cat(1,X,Z);
end
S = score(X,
:
vaxi
if j==1
s
=S;
x
=X;
elseif
(s-S)<O
s =S;
J =j;
x
=X;
end
end
function x2 = getsample(n,p,dosmooth, except)
for j=1:100
x = rand(n,p);
for i=1:p
xl(:,i) = rank(x(:,i),except(:,i));
end
x = xl;
if isequal (dosmooth, 'on')
x = x - rand(size(x));
163
x - 0.5;
x
end
X
x / n;
S = score(X,
);
if j==l1
S = S;
x2 = X;
eoseif (s-S)<0
s = S;
x2 = X;
end
end
function r=rank (x, except)
[sx, rowidx] = sort(x);
r(rowidx) = 1:length(x);
r = r(:);
for i= 1:length(except)
r = r - except(i);
r = nonzeros(r);
r = r + except(i);
end
function s
score(x,crit)
if size(x,1) <2
S = 0;
return
end
switch (crit)
case
c = corrcoef (x);
s = -sum(sum(triu(c,l) .^2));
case
size(x);
[m,p]
pp = (m-1) :-1:2;
I = zeros(m*(m-l)/2,1);
I(cumsum([il pp])) = 1;
I = cumsum(I);
J = ones(m*(m-l)/2,1);
2-pp;
J (cumsum(pp)+i)
J (1)=2;
J = cumsum(J);
d = zeros(size(I));
164
for j=l:p
d = d + (x(I,j)-x(J,j)).^2;
end
s = sqrt(min(d)) ;
end
The output of this function was then saved in a Matlab® data file called Sample2.mat.
The following task is to create the set of RELAP5-3D® input decks corresponding to
each realization of the sample. The following algorithm takes the data saved in
Sample2.mat and creates each input deck from the nominal case saved on file Final36.i
clear
clc
load
lookfor = c
lookfor{l}
lookfor{2}
lookfor{3 }
lookfor{4}
lookfor{5}
lookfor{6}
lookfor{7}
lookfor{8}
lookfor{9}
lookfor{10}
lookfor{11}
lookfor{12}
lookfor {(13}
lookfor {14}
lookfor{15}
lookfor{16}
lookfor{17}
lookfor{18}
lookfor{19}
lookfor{20}
lookfor{21}
lookfor{22}
lookfor{23}
lookfor{24}
lookfor{25}
lookfor{26}
lookfor{27}
lookfor{28}
lookfor{29}
ell
(15, 1);
=
=
=
=
. " .
=
=
=
=
=
cont = 1;
fon = fopen( ' i
I'
1-2 A
J
A
)..M .. );
while feof(fon)<l
C{cont} = fgetl(fon);
cont = cont + 1;
end
fclose(fon);
165
for i=1:256
fid
fopen(strcat(
. .......,num2str(i),
for j=l:length(C);
line = C{j};
if length(line)>=8;
switch line(1:8)
case
{lookfor{l},lookfor{2},lookfor{3},lookfor{4},lookfor{5},...
lookfor{6} };
value =
line = strcat(line);
line = strrep(line, value, sprintf(
Sample{2,1}(i)));
fprintf(fid,
,line);
case lookfor{7};
value = '0.
line = strcat(line);
line = strrep(line, value, sprintf("
Sample{2,2}(i) '));
fprintf(fid, :::. ,line);
case lookfor{8};
value =
line = strcat(line);
line = strrep(line, value, sprintf(-.
Sample{2,3}(i)));
fprintf(fid,
,line);
case {lookfor{9],lookfor{O1},lookfor{ll};
value =
.0 ';
line = strcat(line);
line = strrep(line, value, sprintf('..
Sample{2,4}(i)));
fprintf(fid, '%s",i',line);
case
{lookfor{12},lookfor{13}, lookfor{14}, lookfor{15}, lookfor{16},
lookfor{17}, lookfor{18}, lookfor{19} };
value = '.0
';
line = strcat(line);
line = strrep(line, value, sprintf(' 0..uI
Sample{2,5}(i)));
fprintf (fid, 'Js 1',1•
, ine);
case
{lookfor{20}, lookfor{21}, lookfor{22}, lookfor{23}, lookfor{24},
lookfor{25}, lookfor{26}, lookfor{27}};
value = '". ';
line = strcat(line);
line = strrep(line, value, sprintf('%0).'I
Sample{2,5}(i)));
fprintf(fid, '%s',n' ,line);
case lookfor{28};
value = '1.00 ';
line = strcat(line);
line = strrep(line, value, sprintf('%0'.:,
Sample{2,6}(i)));
fprintf (fid,'sn' line);
case lookfor{29};
166
value =
line = strcat(line)
line = strrep(line, value, sprintf(
Sample{2,7}(i)))
fprintf(fid,
otherwise
fprintf(fid,
,line);
,line);
end
else
fprintf(fid,
,line);
end
end
fclose(fid)
end
Then every case is simulated. After that, the following algorithm imports the data from
the simulation output file (e.g. Trial N.p) to Matlab® environment and saves it into
Results.mat as variables called Trial N.
for k=1:128;
varname = genvarname[
target
[
i
final = ['
,varname, '
eval([final]);
save(' Ieu.'
, varname,
clear(varname,
.dng )
,num2str(k)]);
;<:,
<{
e :::.
'?; s
•i
,num2str (k) ,
1ner
;
end
The output of function cntrlvaro is a matrix where each column is a vector containing the
time evolution of one parameter of the system. The name of the corresponding parameter
is saved in the respective element index of vector "headings". The cntrlvaro function is
the following:
function [cntrl, headings]=cntrlvar(file)
u = 0;
up = 0;
count = 1;
matrix = -1;
flag = 0;
L( Il7
t
IIKI
"'-
fid = fopen(file);
while feof(fid)<l
line = fgetl(fid);
if length(line)>=12
if line(l:12)
'
MI.O
flag = flag + 1;
end
end
if flag == 1 & isempty(line)
flag = 0;
E I
167
break;
end
if flag
--
1
if line(l:6)
up = up + 1;
end
end
end
sections = up;
flag = 0;
fclose(fid);
fid = fopen(file);
flag2 = 0;
up = 0;
while feof(fid)<l
line = fgetl(fid);
if length (line)>=12
if line(l:12) -flag = 1;
end
end
if flag == 1
if line(l:6)
headl = line;
head2 = fgetl(fid);
head3 -= fgetl(fid);
head4 = fgetl(fid);
up = up + 1;
flag2 = 1;
end
if flag2 == 1;
head{up*4-3,1} = headl;
head{up*4-2,1} = head2;
head{up*4-1,1} = head3;
head{up*4,1} = head4;
flag2 = 0;
end
if up == sections & flag == 1 &
not(isempty(str2num(line(1:14))))
leng = length(line);
flag = 0;
break;
end
end
end
switch leng
case 27
lastsecthead = 1;
case 40
lastsecthead = 2;
case 53
lastsecthead = 3;
case 66
168
lastsecthead
4;
case 79
lastsecthead
5;
case 92
lastsecthead = 6;
case 105
lastsecthead = 7;
case 118
lastsecthead =8;
case 131
lastsecthead = 9;
end
headings {1,} =
cat(2,head{1, 1} (1:14),head{2,1} (1:14),head{3,1} (1:14),head{4,1)
} (1:14));
for i=1:sections-1
for j=1 :9
headings{1,1+(i*9)-(9-j)} = cat(2,head{i*4-3}(15+13*(j1):15+13*j- )..1)
.
head{i*4-2}(15+13*(j-1):15+13*j-1),...
head{i*4-1}(15+13*(j-1):15+13*j-1),...
head{i*4}(15+13*(j-1):15+13*j-1));
end
end
for i=sections:sections
for j=1 :lastsecthead
headings{1,1+(i*9)-(9-j)} -= cat(2,head{i*4-3}(15+13*(j1):15+13*j-1) ,...
head{i*4-2}(15+13*(j-1):15+13*j-1),...
head{i*4-1}(15+13*(j-1):15+13*j-1),...
head{i*4}(15+13*(j-1):15+13*j-1));
end
end
flag = 0;
fclose(fid);
fid = fopen(file);
while feof(fid)<l
line = fgetl(fid);
if length(line)>=12
if line(1:12) ==
flag = 1;
end
end
if isempty(line)
flag = 0;
elseif length(line) >= 33
if line(l:33) ==
flag = 0;
end
end
if length(line) >= 7
if line(1:7) ==
flag = 0;
end
end
if flag ==1 & line(1:6) ==
169
u = u + 1;
if u == sections + 1;
1;
u
end
if
flag =
if flag
1 & length(line) > 14 &
1 &- length(line) > 14&
not(isempty(str2num(line (1:14))));
if max(matrix(:,l)) <str2num(line(l:14))
matrix(count, 1) = str2num(line(1:14));
matrix(count,2) = str2num(line(15:27));
matrix(count,3) = str2num(line(28:40));
matrix(count,4) = str2num(line(41:53));
matrix(count,5) = str2num(line(54:66));
matrix(count,6) = str2num(line(67:79));
matrix(count,7) = str2num(line(80:92));
matrix(count,8) = str2num(line(93:105));
matrix(count,9) = str2num(line(106:118));
matrix(count, IC )= str2num(line(119:131));
count = count 4
elseif u == sectior
x = find(matrix(:,l) = str2num(line(l:14)));
y = (u-l)*9 + 2;
if lastsecthead >= 1
str2num(line(15:27));
matrix(x,y)
if lastsecthead >= 2
matrix(x,y+l) = str2num(line(28:40));
if lastsecthead >= 3
matrix(x,y+2) = str2num(line(41:53));
if lastsecthead >= 4
matrix(x,y+3) = str2num(line(54:66));
if lastsecthead >= 5
matrix(x,y+4) = str2num(line(67:79));
if lastsecthead >= 6
matrix(x,y+5) =
str2num(line(80:92));
if lastsecthead >= 7
matrix(x,y+6) =
str2num(line(93:105));
if lastsecthead >= 8
matrix(x,y+7) =
8
));
str2num(line(106:ll
if lastsecthead >= 9
matrix(x,y+8) =
str2num(line(119:131));
end
end
end
end
end
end
end
end
end
else
x -= find(matrix(:,l) == str2num(line(l:1
y = (u-l)*9 + 2;
= str2num(line(15: 2 7 ));
matrix(x,y)
170
4
)));
matrix (x, y+l)
matrix(x,y+2)
matrix(x,y+3)
matrix (x, y+4)
matrix(x,y+5)
matrix (x, y+6)
matrix (x,y+7)
matrix(x,y+8)
=
=
=
=
=
=
=
str2num(line(28:40));
str2num(line(41:53));
str2num(line(54:66));
str2num(line(67:79));
str2num(line(80:92));
str2num(line(93:105))
str2num(line(106:118)
str2num(line(119:131))
end
end
end
cntrl = matrix;
fclose(fid);
After the data is imported and saved, the analysis starts. The following algorithm tests a
certain parameter against a given limit and returns a vector "Failures", with a "0" if a
realization was a success or a "1"if it was a failure when compared to the limit. The
realization number corresponds to the indices of the "Failures" vector. The algorithm also
plots time evolutions of the parameter for all realizations in the sample.
Trial = whos('',
,
Longitud = length(Trial);
Failures = zeros(128,1);
limit = 1600
'J.
for i=l:Longitud;
load('P].e,. 14.1,.
.i. Trial (i).name);
);
eval(['pio:
,Trial(i) .name, '
1 ý:,:a::x ,Trial (i) .name,
: :.;
,Trial(
i) .name, ' :,79)
']);
hold
;
L = eval([
e ,
,Trial(i).name,
Z,:
x =
eval([
ma x- ,Trial(i) .name, ' i200:L,:8)),
:
,Trial(i).name1
r",'
Name = Trial(i).name;
if x>(limit+273.15);
Name = Trial(i).name;
Index = str2num(Name(7:length(Name)));
Failures(Index,l) = 1;
end
clear(Trial(i).name);
end
The complete set of data structures generated by these algorithms provide then the
necessary framework for the required further analysis.
171
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